Alcohol-based fuel reaction device

By designing an alcohol-based fuel reaction device including a temperature control unit and a catalyst assembly, the inefficiency problem caused by temperature deviation when the synthesis gas generates alcohol-based fuel in the reaction tank is solved, and more efficient alcohol-based fuel synthesis is achieved.

CN119588253APending Publication Date: 2025-03-11中节能节能科技有限公司
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Patent Information

Application Number
CN202411916912.3
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2024-12-24
Publication Date
2025-03-11

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Abstract

The invention discloses an alcohol-based fuel reaction device, which relates to the field of alcohol-based fuels, and comprises a reaction tank, two groups of partition plates respectively arranged at the upper end and the lower end of the reaction tank; the temperature control unit is arranged between the two groups of partition plates in the reaction tank; the plurality of groups of reaction units are uniformly arranged between the two groups of partition plates; the temperature control unit comprises a water inlet and a water outlet, and a heat exchanger is connected between the water inlet and the water outlet through a pipeline; the water flow layering part is arranged in the reaction tank, continuous heat exchange can be conducted on the reaction temperature of the reaction pipe through the temperature control unit, so that the reaction temperature in the reaction pipe is kept at a proper temperature all the time, meanwhile, circulation of water flow in the reaction tank can be achieved through the water flow layering arrangement of the temperature control unit, and therefore heat exchange is better achieved; and the actual effect of heat exchange is further improved.
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Description

Technical Field

[0001] The invention relates to the technical field of alcohol-based fuels, in particular to an alcohol-based fuel reaction device. Background Art

[0002] Against the backdrop of growing global energy demand and unstable oil supply, crude oil prices have accelerated. In order to cope with resource crises, reduce environmental pollution and improve economic efficiency, countries are actively researching and developing new energy sources, including green alcohol-based fuels. As we all know, biomass-based alcohol fuels and carbon-containing industrial tail gas-based alcohol fuels have many advantages of resource regeneration, sustainability and environmental friendliness. Therefore, in recent years, research on syngas-based alcohol fuels and efficient and clean utilization has received more and more attention.

[0003] At present, since the synthesis gas releases heat when it generates alcohol-based fuel in the reaction tank, and this method of synthesizing alcohol-based fuel requires a suitable temperature, when the temperature deviation in the reaction tank is large, the efficiency of the synthesized alcohol-based fuel will be low. For this reason, we have designed an alcohol-based fuel reaction device.

[0004] The above contents are only used to assist in understanding the technical solution of the present invention, and do not constitute an admission that the above contents are the closest prior art. Summary of the invention

[0005] The purpose of the present invention is to provide an alcohol-based fuel reaction device to solve the problem proposed in the above background technology that when the synthesis gas is used to generate alcohol-based fuel in a reaction tank, heat will be released. At the same time, this method of synthesizing alcohol-based fuel requires a suitable temperature. When the temperature deviation in the reaction tank is large, the efficiency of the synthesized alcohol-based fuel will be low.

[0006] To achieve the above object, the present invention provides the following technical solution: an alcohol-based fuel reaction device, comprising a reaction tank, wherein the upper and lower ends of the reaction tank are respectively provided with a gas phase inlet and a gas phase outlet, and further comprising:

[0007] Two sets of partition plates are respectively arranged at the upper and lower ends of the reaction tank;

[0008] A temperature control unit, disposed between the two groups of partition plates in the reaction tank, for controlling the reaction temperature in the reaction tank;

[0009] A plurality of reaction units are evenly arranged between the two groups of partition plates, and are connected to the gas phase inlet and the gas phase outlet through a connecting pipe through the two groups of partition plates, and gas valves are arranged at the connecting pipe and the gas phase inlet and the gas phase outlet;

[0010] Wherein, the temperature control unit comprises:

[0011] A water inlet is provided on the inner wall of the reaction tank between the two groups of partition plates and is located at the upper end of the reaction tank. A water outlet is provided at the lower end of the reaction tank between the two groups of partition plates. A heat exchanger is connected between the water inlet and the water outlet through a pipeline.

[0012] The water flow stratification part is arranged in the reaction tank, and is used for the water flowing in from the water inlet to flow in layers and cross in the reaction tank, so as to fully contact with the reaction unit and provide the temperature required for the reaction in the reaction unit.

[0013] Preferably, the water flow stratification part includes a plurality of stratification plates, which are evenly distributed from top to bottom in the reaction tank, and each stratification plate is provided with a water flow outlet at one end, and the water flow outlets provided on two adjacent stratification plates are symmetrically provided.

[0014] Preferably, the reaction unit comprises:

[0015] Multiple groups of reaction tubes are arranged between the partition plate and the layer plate and between two adjacent layer plates. The reaction tanks at the uppermost and lowermost ends are connected to the gas phase inlet and the gas phase outlet through the connecting pipes. Two adjacent groups of reaction tubes are connected at one side of the water outlet through a connecting pipe.

[0016] The reaction tube is located at one end of the water outlet and is connected to the inner wall of the reaction tank to form an outlet, and the other end is closed, and the outlet is sealed by a sealing cover;

[0017] The catalyst assembly is arranged in the reaction tube and is used for the reaction gas to pass through the catalyst assembly to be catalyzed to synthesize alcohol-based fuel.

[0018] Preferably, the catalyst assembly comprises:

[0019] A plurality of placement cylinders, slidably disposed on the reaction tube, for placing catalysts;

[0020] The clamping piece is arranged between two adjacent placement tubes and is used for clamping and fixing the two adjacent placement tubes.

[0021] Preferably, the placement tube includes a tube body and a tube cover, the tube body and the tube cover are threadedly connected to each other, and the tube body and the tube cover are both hollow.

[0022] Preferably, the engaging member comprises:

[0023] Two groups of slots are symmetrically arranged on the cylinder cover;

[0024] Two groups of card blocks symmetrically arranged at the tail of the cylinder body of the adjacent placement cylinder and used in conjunction with the card slots, wherein the card blocks are provided with slots;

[0025] The insert rod is set at the position of the slot and the tube cover for limited sliding. The tube cover is provided with a slide groove for limited sliding of the insert rod. A limit plate is set on the insert rod. A spring is sleeved on the insert rod between the limit plate and the slide groove.

[0026] Compared with the prior art, the present invention has the following beneficial effects:

[0027] The present invention can continuously heat exchange the reaction temperature of the reaction tube through the setting of the temperature control unit, so that the reaction temperature in the reaction tube is always maintained at an appropriate temperature. At the same time, the water flow stratification setting of the temperature control unit can realize the circulation of the water flow in the reaction tank, thereby better realizing heat exchange and further improving the actual effect of heat exchange.

[0028] The present invention can increase the reaction time of the synthesis gas in the reaction tank and fully contact the synthesis gas with the catalyst through the layered design of the reaction tubes in the reaction unit. At the same time, through the arrangement of the catalyst assembly, the catalyst can be replaced without stopping the machine. BRIEF DESCRIPTION OF THE DRAWINGS

[0029] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0030] Figure 2 This is a cross-sectional view of the interior of the reaction tank of the present invention;

[0031] Figure 3 It is a partial cross-sectional connection diagram of the entire reaction tube of the present invention;

[0032] Figure 4 This is a schematic diagram of two adjacent placement tubes of the present invention;

[0033] Figure 5 This is a cross-sectional view of the clamping member of the placement tube of the present invention;

[0034] Figure 6 for Figure 4 Enlarged view of point A in the middle;

[0035] Figure 7 for Figure 5 Enlarged view of point B in the middle;

[0036] Figure 8 A distribution diagram for placing the catalyst layer inside the cylinder.

[0037] Figure numerals: 1-reaction tank; 2-gas phase inlet; 3-gas phase outlet; 4-partition plate; 5-temperature control unit; 51-water inlet; 52-water outlet; 53-layering plate; 54-water outlet; 6-reaction unit; 61-reaction tube; 62-outlet; 63-placing tube; 631-tube body; 632-tube cover; 64-clamping part; 641-slot; 642-block; 643-slot; 644-insertion rod; 645-slide; 646-limiting plate; 647-spring; 65-connecting tube. DETAILED DESCRIPTION

[0038] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0039] Embodiment 1

[0040] See also Figure 1-8 The present invention provides a technical solution: an alcohol-based fuel reaction device, comprising a reaction tank 1, wherein the upper and lower ends of the reaction tank 1 are respectively provided with a gas phase inlet 2 and a gas phase outlet 3, characterized in that it also includes:

[0041] Two sets of partition plates 4 are respectively arranged at the upper and lower ends of the reaction tank 1;

[0042] A temperature control unit 5 is disposed between two groups of partition plates 4 in the reaction tank 1 and is used to control the reaction temperature in the reaction tank 1;

[0043] Multiple groups of reaction units 6 are evenly arranged between the two groups of partition plates 4, and are connected to the gas phase inlet 2 and the gas phase outlet 3 through the connecting pipe through the two groups of partition plates 4, and the connecting pipe and the gas phase inlet 2 and the gas phase outlet 3 are provided with gas valves;

[0044] Wherein, the temperature control unit 5 comprises:

[0045] A water inlet 51 is provided on the inner wall of the reaction tank 1 between the two groups of partition plates 4 and is located at the upper end of the reaction tank 1. A water outlet 52 is provided at the lower end of the reaction tank 1 between the two groups of partition plates 4. A heat exchanger is connected between the water inlet 51 and the water outlet 52 via a pipeline.

[0046] The water flow stratification part is arranged in the reaction tank 1 , and is used for the water flowing in from the water inlet 51 to flow in layers and cross in the reaction tank 1 , so as to fully contact with the reaction unit 6 , and provide the required temperature for the reaction in the reaction unit 6 .

[0047] The water flow stratification part includes multiple layers of stratification plates 53, which are evenly distributed from top to bottom in the reaction tank 1. A water flow outlet 54 is opened at one end of each layer of the stratification plates 53, and the water flow outlets 54 opened on two adjacent layers of the stratification plates 53 are opened symmetrically.

[0048] In addition, the reaction unit 6 comprises:

[0049] Multiple groups of reaction tubes 61 are arranged between the partition plate 4 and the layer plate 53 and between two adjacent layer plates 53. The reaction tanks 1 at the uppermost and lowermost ends are connected to the gas phase inlet 2 and the gas phase outlet 3 through the connecting pipes. Two adjacent reaction tubes 61 are connected at one side of the water outlet 54 through the connecting pipe 65.

[0050] It should be noted that a thermometer is provided in the connecting pipe 65 to detect the reaction temperature in the reaction tube 61 and the connecting pipe 65 in real time to ensure that the reaction temperature is at the optimum temperature (generally 260 degrees Celsius with a deviation of about 10 degrees). Since the reaction of synthesizing alcohol-based fuel is an exothermic reaction, when the temperature in the reaction tube 61 is higher than the optimum temperature, the temperature control unit 5 starts to work and cools the reaction tube 61 by heat exchange. At the same time, the temperature control unit 5 can work in a cycle, so as to ensure that the temperature in the reaction tube 61 is always maintained in the optimum temperature range;

[0051] The reaction tube 61 is located at one end of the water outlet 54 and is connected to the inner wall of the reaction tank 1 to form an outlet 62, and the other end is closed. The outlet 62 is sealed by a sealing cover;

[0052] The catalyst assembly is disposed in the reaction tube 61 and is used for catalyzing the reaction gas through the catalyst assembly to synthesize the alcohol-based fuel.

[0053] Meanwhile, the catalyst assembly comprises:

[0054] A plurality of placement cylinders 63, slidably disposed on the reaction tube 61, for placing catalysts;

[0055] The engaging member 64 is disposed between two adjacent placement tubes 63 and is used for engaging and fixing the two adjacent placement tubes 63 .

[0056] In addition, the placement tube 63 includes a tube body 631 and a tube cover 632. The tube body 631 and the tube cover 632 are threadedly connected to each other. The tube body 631 and the tube cover 632 are both hollowed out for gas to pass through.

[0057] At the same time, the engaging member 64 includes:

[0058] Two groups of slots 641 are symmetrically arranged on the cylinder cover 632;

[0059] Two groups of clamping blocks 642 symmetrically arranged at the tail of the cylinder body 631 of the adjacent placement cylinder 63 and used in conjunction with the clamping slot 641, wherein the clamping blocks 642 are provided with slots 643;

[0060] The plug rod 644 is provided at the position of the slot 641 and the tube cover 632 for limited sliding. The tube cover 632 is provided with a slide groove 645 for limited sliding of the plug rod 644. The plug rod 644 is provided with a limit piece 646. The plug rod 644 between the limit piece 646 and the slide groove 645 is sleeved with a spring 647.

[0061] It should be noted that when the catalyst is replaced, there is no need to stop the machine for replacement. You only need to close the gas valves at the connecting pipes on a group of reaction tubes 61 in turn, then open the sealing cover to extract the placement tube 63, and then place the reaction tube containing the new catalyst in the reaction tube 61. You can replace them in turn without stopping the machine.

[0062] Embodiment 2

[0063] The difference between this embodiment and embodiment 1 is that this embodiment also provides a synthesis process for preparing alcohol-based fuel using an alcohol-based fuel reaction device, comprising the following steps:

[0064] Step 1: After the synthesis gas rich in hydrogen, carbon monoxide and carbon dioxide is purified (solid impurities in the synthesis gas are removed), it is sent to the reaction unit 6 in the reaction tank 1 through the gas phase inlet 2;

[0065] Step 2: Collect the pure water formed after being treated by the water treatment unit, then electrolyze the pure water to separate hydrogen and pass it into the reaction tank 1 through the gas phase inlet 2;

[0066] Step 3, place the catalyst in the cylinder body 631 with the cylinder cover 632 opened, and then tighten it by screwing, fill multiple placement cylinders 63 with catalyst in turn, then connect two placement cylinders 63 through the snap-fit ​​piece 64, and then insert the previous placement cylinder 63 into the reaction tube 61 from the outlet 62, connect one placement cylinder 62 to another until the entire reaction tube 61 is filled, and insert the placement cylinder 63 into all reaction tubes 61 in turn, and finally seal the outlet 62 with a sealing cover;

[0067] Step 4: Water of the required temperature for the reaction is introduced from the water inlet 51, and then the water flows through each layer plate 53 in sequence until the space inside the reaction tank 1 between the partition plates 4 is filled so that the water is fully in contact with each layer of the reaction tube 61. After the water flows out from the water outlet 52, the water temperature is adjusted by the heat exchanger, and then the water is sent in again from the water inlet 51 to realize the water circulation;

[0068] Step 5: The synthesis gas introduced into the gas phase inlet 2 reacts under high temperature, high pressure and catalytic conditions of the catalyst to generate gaseous alcohol-based fuel and water, which are finally discharged from the gas phase outlet 3;

[0069] Step 6: Separate the gaseous alcohol-based fuel and water as well as the unreacted carbon monoxide, carbon dioxide and hydrogen, and send the unreacted carbon monoxide, carbon dioxide and hydrogen back into the reaction tank 1.

Claims

1. An alcohol-based fuel reaction device, comprising a reaction tank (1), wherein the reaction tank (1) is provided with a gas phase inlet (2) and a gas phase outlet (3) at the upper and lower ends thereof, respectively, wherein: Also includes: Two groups of partition plates (4) are respectively arranged at the upper and lower ends of the reaction tank (1); A temperature control unit (5), arranged between the two groups of partition plates (4) in the reaction tank (1), and used for controlling the reaction temperature in the reaction tank (1); A plurality of reaction units (6) are evenly arranged between the two groups of partition plates (4) and are connected to the gas phase inlet (2) and the gas phase outlet (3) through connecting pipes through the two groups of partition plates (4), and gas valves are arranged at the connecting pipes and the gas phase inlet (2) and the gas phase outlet (3); Wherein, the temperature control unit (5) comprises: A water inlet (51) is provided on the inner wall of the reaction tank (1) between the two groups of partition plates (4) and is located at the upper end of the reaction tank (1); a water outlet (52) is provided at the lower end of the reaction tank (1) between the two groups of partition plates (4); a heat exchanger is connected between the water inlet (51) and the water outlet (52) via a pipeline; The water flow stratification section is arranged in the reaction tank (1) and is used for the water flowing in from the water inlet (51) to flow in layers and cross in the reaction tank (1) so as to fully contact with the reaction unit (6) and provide the temperature required for the reaction in the reaction unit (6).

2. An alcohol-based fuel reaction device according to claim 1, characterized in that: The water flow stratification part comprises a plurality of stratification plates (53) which are evenly distributed from top to bottom in the reaction tank (1); a water flow outlet (54) is provided at one end of each stratification plate (53); and the water flow outlets (54) provided on two adjacent stratification plates (53) are symmetrically provided.

3. An alcohol-based fuel reaction device according to claim 2, characterized in that: The reaction unit (6) comprises: A plurality of groups of reaction tubes (61) are arranged between the partition plate (4) and the layer plate (53) and between two adjacent layer plates (53); the reaction tanks (1) at the uppermost and lowermost ends are connected to the gas phase inlet (2) and the gas phase outlet (3) through the connecting pipes; and two adjacent groups of reaction tubes (61) are connected at one side of the water outlet (54) through a connecting pipe (65); The reaction tube (61) is located at one end of the water outlet (54) and is connected to the inner wall of the reaction tank (1) to form an outlet (62), and the other end is closed. The outlet (62) is sealed by a sealing cover; The catalyst assembly is arranged in the reaction tube (61) and is used for the reaction gas to pass through the catalyst assembly to undergo catalysis to synthesize alcohol-based fuel.

4. An alcohol-based fuel reaction device according to claim 3, characterized in that: The catalyst assembly comprises: A plurality of placement cylinders (63) are slidably disposed on the reaction tube (61) and are used to place catalysts; The engaging member (64) is arranged between two adjacent placement tubes (63) and is used for engaging and fixing the two adjacent placement tubes (63).

5. The alcohol-based fuel reaction device according to claim 4, characterized in that: The placement tube (63) comprises a tube body (631) and a tube cover (632), wherein the tube body (631) and the tube cover (632) are threadedly connected to each other, and both the tube body (631) and the tube cover (632) are hollowed out.

6. The alcohol-based fuel reaction device according to claim 5, characterized in that: The engaging member (64) comprises: Two groups of clamping grooves (641) are symmetrically arranged on the cylinder cover (632); Two groups of card blocks (642) symmetrically arranged at the tail of the cylinder body (631) of the adjacent placement cylinder (63) and used in conjunction with the card slot (641), wherein the card blocks (642) are provided with slots (643); The insert rod (644) is arranged at the position of the slot (641) and the tube cover (632) for limited sliding. The tube cover (632) is provided with a slide groove (645) for limited sliding of the insert rod (644). A limit plate (646) is arranged on the insert rod (644). A spring (647) is sleeved on the insert rod (644) between the limit plate (646) and the slide groove (645).