CN204404423U - Based on the air-conditioning system of methanol-water preparing hydrogen, generating power system - Google Patents
Based on the air-conditioning system of methanol-water preparing hydrogen, generating power system Download PDFInfo
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- CN204404423U CN204404423U CN201420846781.1U CN201420846781U CN204404423U CN 204404423 U CN204404423 U CN 204404423U CN 201420846781 U CN201420846781 U CN 201420846781U CN 204404423 U CN204404423 U CN 204404423U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
The utility model discloses a kind of air-conditioning system based on methanol-water preparing hydrogen, generating power system, comprise methanol-water reformation hydrogen production equipment, fuel cell and thermoelectricity hybrid air-conditioning equipment; Methanol-water reformation hydrogen production equipment, for the reaction of first alcohol and water generation reformation hydrogen production, the hydrogen that reformation hydrogen production reaction obtains flows to fuel cell, and in the process of reformation hydrogen production reaction, the heat delivery in the waste gas of discharge is to heat absorption type refrigeration unit; Fuel cell, produce electric energy for hydrogen and oxygen generation electrochemical reaction, the electric energy of generation is for power with electric-type air-conditioning unit; Thermoelectricity hybrid air-conditioning equipment, comprise heat absorption type refrigeration unit and use electric-type air-conditioning unit, heat absorption type refrigeration unit Absorbable rod methanol-water reformation hydrogen production equipment discharge waste gas in heat and freeze, with electric-type air-conditioning unit can consume fuel battery produce electric energy and freeze.The utility model environmental protection, energy-conservation, convenient, by region and ambient influnence little, and methanol-water raw material capacity usage ratio is high.
Description
Technical field
The utility model relates to air-conditioning system technical field, particularly a kind of air-conditioning system based on methanol-water preparing hydrogen, generating power system.
Background technology
Air-conditioning and air conditioning (air conditioning), mainly refer to the process of the parameters such as the temperature of building/structures environment air being carried out to regulation and control, to create suitable living condition or the technology of condition of work.In the prior art, air-conditioning needs access civil power just can work usually, and for not having the place of power supply, then cannot work.
In view of this, this creator has applied for a patent application 201410141289.9(applicant on April 10th, 2014: Shanghai Hejide Dynamic Hydrogen Machine Co., Ltd.), this patent application discloses a kind of methanol-water reformation electricity generation air conditioner system and control method, comprise methanol-water reformation hydrogen production equipment, generating equipment and air-conditioning equipment, wherein, the hydrogen that methanol-water reformation hydrogen production equipment is obtained, flow to generating equipment and generate electricity, the electric energy of generation is that air-conditioning equipment is powered.Adopt this technical scheme that air-conditioning can be made in the place not having power supply, still can normally work, without the need to additional power supply.
But, the utilization rate of above-mentioned air-conditioning system to methanol-water energy is on the low side, usually 36%-50% is only had, concrete reason is as follows: methanol-water reformation hydrogen production equipment is in running, the reformation hydrogen production of main generation methyl alcohol and water reacts, catalyst is passed through under the pressure condition of i.e. methyl alcohol and steam 1-5M Pa at 350-409 DEG C of temperature, under the effect of catalyst, there is the transformationreation of methanol decomposition reaction and carbon monoxide, generate hydrogen and carbon dioxide, this is the gas solid catalytic reaction system of component more than, many reactions.Reaction equation is: (1) CH
3oH → CO+2H
2; (2) H
2o+CO → CO
2+ H
2; (3) CH
3oH+H
2o → CO
2+ 3H
2; The catalytic reaction of methanol-water completes in the reformer of reforming methanol water hydrogen producer, reformer comprises reformer housing and is positioned at combustion chamber and the reformer chamber of reformer housing, usually, the temperature of 350-409 DEG C is needed in reformer chamber, and in combustion chamber, needing the temperature of 405-570 DEG C, reformer could normal work.And the temperature of 405-570 DEG C in combustion chamber will be maintained, then need the obtained hydrogen of a part to burn to maintain reformer in a combustion chamber and run.Combustion chamber is in the process of combustion of hydrogen, and the waste gas (nitrogen in air, carbon dioxide, aqueous vapor etc.) of generation is directly discharged from the chimney of reformer.Because these waste gas are high-temp waste gas, therefore, the discharge of waste gas causes the loss of energy, and the energy of this part loss has accounted for the 25%-40% of methanol-water energy, thus makes the utilization rate of above-mentioned air-conditioning system to methanol-water energy on the low side.
Utility model content
The technical problems to be solved in the utility model is for above-mentioned deficiency of the prior art, provides a kind of environmental protection, energy-conservation, convenient, by region and ambient influnence little, and the air-conditioning system based on methanol-water preparing hydrogen, generating power system that capacity usage ratio is high.
For solving the problems of the technologies described above, the technical solution of the utility model is:
Based on an air-conditioning system for methanol-water preparing hydrogen, generating power system, comprise methanol-water reformation hydrogen production equipment, fuel cell and thermoelectricity hybrid air-conditioning equipment, wherein:
Methanol-water reformation hydrogen production equipment, react for first alcohol and water generation reformation hydrogen production, the hydrogen that reformation hydrogen production reaction obtains flows to fuel cell, and in the process of reformation hydrogen production reaction, the heat delivery in the waste gas of discharge is to the heat absorption type refrigeration unit of thermoelectricity hybrid air-conditioning equipment;
Fuel cell, produces electric energy for hydrogen and oxygen generation electrochemical reaction, and the electric energy of generation is that the use electric-type air-conditioning unit of thermoelectricity hybrid air-conditioning equipment is powered;
Thermoelectricity hybrid air-conditioning equipment, comprise heat absorption type refrigeration unit and use electric-type air-conditioning unit, heat absorption type refrigeration unit Absorbable rod methanol-water reformation hydrogen production equipment discharge waste gas in heat and freeze, with electric-type air-conditioning unit can consume fuel battery produce electric energy and freeze.
Described heat absorption type refrigeration unit comprises generator, condenser, first throttle valve, evaporimeter, absorber, solution heat exchanger and solution pump, wherein:
Generator, seethes with excitement concentrated for making the rare liquation of lithium bromide brought from absorber absorb the heat the waste gas of described methanol-water reformation hydrogen production equipment discharge, produces high pressure refrigerant vapor and the dense liquation of lithium bromide; High pressure refrigerant vapor flows to condenser, and the dense liquation of lithium bromide flows to absorber after solution heat exchanger heat exchange;
Condenser, is condensed into high pressure refrigerant liquid for high pressure refrigerant vapor, and the condenser heat discharged is taken away by cooling medium; The refrigerant liquid of high pressure refrigerant liquid under the throttling of first throttle valve is evaporating pressure, enters evaporimeter;
Evaporimeter, for the heat absorption of refrigerant liquid carburation by evaporation, produce refrigerating capacity, the low-pressure steam of evaporation enters absorber;
Absorber, carries the low-pressure steam of coming from evaporimeter for making to carry the bromize lithium concentrated solution of coming to absorb from generator, produces bromize lithium dilute solution;
Solution pump, for being pumped to generator by the bromize lithium dilute solution in absorber; In pumping procedure, this bromize lithium dilute solution through described solution heat exchanger, liquation heat exchange dense with lithium bromide.
Described methanol-water reformation hydrogen production equipment comprises methanol-water reservoir vessel, raw material conveying device, reformer and membrane separation device; Described raw material conveying device connects methanol-water reservoir vessel and reformer respectively by conveyance conduit, this raw material conveying device by the methanol-water feedstock transportation in methanol-water reservoir vessel to reformer; Described reformer comprises heat exchanger, vaporizer, reformer chamber, separation chamber and exhaust emission device, and described membrane separation device is arranged in separation chamber, and separation chamber is arranged at the top of reformer chamber; Described methanol-water raw material enters vaporizer vaporization in heat exchanger after heat exchange; Methanol steam after vaporization and water vapour enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300-420 DEG C, and the temperature on described reformer chamber top is 400-570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350-570 DEG C, obtains hydrogen from the aerogenesis end of the membrane separation device in separation chamber; The hydrogen partial that described reformer is obtained is or/and residual air maintains reformer operation by burning, and the waste gas produced after burning is expelled to described heat absorption type refrigeration unit by exhaust emission device.
Described membrane separation device is the membrane separation device at porous ceramic surface Vacuum Deposition palladium-silver, and film plating layer is palladium-silver, and the mass percent palladium of palladium-silver accounts for 75%-78%, and silver accounts for 22%-25%.
Described reformer one end is provided with starting drive, and this starting drive comprises cup, cup is provided with raw material input channel, heating and gasifying pipeline, igniter and temperature detection device; Described raw material input channel can input first alcohol and water raw material, and raw material input channel is connected with heating and gasifying pipeline, and first alcohol and water raw material enters after heating and gasifying pipeline through raw material input channel, exports from the end of heating and gasifying pipeline; The position of described igniter is corresponding with the end of heating and gasifying pipeline, for lighting a fire to the first alcohol and water raw material exported in heating and gasifying pipeline, first alcohol and water raw material is through ignition device after-combustion, can heat heating and gasifying pipeline, make heating and gasifying ducted first alcohol and water material gasification and strengthen rapidly combustion intensity, and then being reformer heating; Described temperature detection device is for detecting the other temperature of heating and gasifying pipeline; After described reformer starts hydrogen manufacturing, the hydrogen partial that reformer is obtained is or/and residual air is run by burning maintenance reformer.
Described cup comprises the liquid containing portion above installation portion and installation portion, described raw material input channel, heating and gasifying pipeline, igniter and temperature detection device are all installed on the installation portion of cup, described liquid containing portion can hold the first alcohol and water raw material exported from heating and gasifying pipe end, and described liquid containing portion upper end is also provided with liquid Splashproof cover.
Described heating and gasifying pipeline comprises straight-through pipeline section, pigtail and upper arch pipeline section successively, and described first alcohol and water raw material after straight-through pipeline section rises to extreme higher position, then can decline through pigtail spiral, then exports after upper arch pipeline section.
The bottom side of described cup is provided with air intake cover plate, and this air intake cover plate is provided with air channel, and outside air can enter in reformer through this air channel; Described raw material input channel is provided with magnetic valve, opens or closes to control raw material input channel.
The beneficial effects of the utility model are: one, the utility model air-conditioning system without the need to coal combustion, oil, natural gas and common coal gas, but adopt clean energy resource methyl alcohol and water, thus very environmental protection; Two, the utility model air-conditioning system adopts clean energy resource methyl alcohol and water, its cost significantly lower than civil power, good economy performance; Three, the utility model air-conditioning system is not by regional impact, and in office where territory can be set up, very convenient; Four, the utilization rate of the utility model methanol-water energy is high, on the one hand, the electricity that the use electric-type air-conditioning unit of thermoelectricity hybrid air-conditioning equipment can utilize fuel cell to produce freezes, on the other hand, the heat absorption type refrigeration unit of thermoelectricity hybrid air-conditioning equipment can utilize the heat in the waste gas of methanol-water hydrogen producer to freeze, thus makes the utilization rate of methanol-water energy high.
Accompanying drawing explanation
Fig. 1 is overall structure block diagram of the present utility model.
Fig. 2 is the block diagram of heat absorption type refrigeration unit of the present utility model.
Fig. 3 is the overall structure block diagram of the utility model one preferred embodiment.
Fig. 4 is the dispersed structure schematic diagram of reformer.
Fig. 5 is the overall structure schematic diagram of reformer starting drive.
Fig. 6 is the cup holder portion structural representation of reformer starting drive.
Detailed description of the invention
Below in conjunction with accompanying drawing, structural principle of the present utility model and operation principle are described in further detail.
As shown in Figure 1, a kind of air-conditioning system based on methanol-water preparing hydrogen, generating power system, comprises methanol-water reformation hydrogen production equipment 1, fuel cell 2 and thermoelectricity hybrid air-conditioning equipment 3, wherein:
Methanol-water reformation hydrogen production equipment 1, react for first alcohol and water generation reformation hydrogen production, the hydrogen that reformation hydrogen production reaction obtains flows to fuel cell 2, and in the process of reformation hydrogen production reaction, the heat delivery in the waste gas of discharge is to the heat absorption type refrigeration unit 31 of thermoelectricity hybrid air-conditioning equipment 3;
Fuel cell 2, produces electric energy for hydrogen and oxygen generation electrochemical reaction, and the electric energy of generation is that the use electric-type air-conditioning unit 32 of thermoelectricity hybrid air-conditioning equipment 3 is powered;
Thermoelectricity hybrid air-conditioning equipment 3, comprise heat absorption type refrigeration unit 31 and with electric-type air-conditioning unit 32, heat absorption type refrigeration unit 31 Absorbable rod methanol-water reformation hydrogen production equipment 1 discharge waste gas in heat and freeze, with electric-type air-conditioning unit 32 can consume fuel battery 2 produce electric energy and freeze.
After adopting thermoelectricity hybrid air-conditioning equipment, the utilization rate of methanol-water energy increases substantially, on the one hand, the electricity that the use electric-type air-conditioning unit of thermoelectricity hybrid air-conditioning equipment can utilize fuel cell to produce freezes, on the other hand, the heat absorption type refrigeration unit of thermoelectricity hybrid air-conditioning equipment can utilize the heat in the waste gas of methanol-water hydrogen producer to freeze, thus makes the utilization rate of methanol-water energy high.Such as: if the heat in waste gas has accounted for 30% of the methanol-water energy expended, the electric energy that fuel cell produces has accounted for 45% of the methanol-water energy expended, and so, the methanol-water capacity usage ratio of the utility model air-conditioning system will increase substantially to 75%.
As shown in Figure 2, described heat absorption type refrigeration unit 31 comprises generator 311, condenser 312, first throttle valve 313, evaporimeter 314, absorber 315, solution heat exchanger 316 and solution pump 317, wherein:
Generator 311, seethes with excitement concentrated for making the rare liquation of lithium bromide of coming from absorber 315 pumping absorb the heat the waste gas of described methanol-water reformation hydrogen production equipment 1 discharge, produces high pressure refrigerant vapor and the dense liquation of lithium bromide; High pressure refrigerant vapor flows to condenser 312, and the dense liquation of lithium bromide flows to absorber 315 after solution heat exchanger 316 heat exchange;
Condenser 312, is condensed into high pressure refrigerant liquid for high pressure refrigerant vapor, and the condenser heat discharged is taken away by cooling medium, and this cooling medium is preferably cooling water; The refrigerant liquid of high pressure refrigerant liquid under first throttle valve 313 throttling is evaporating pressure, enters evaporimeter 314;
Evaporimeter 314, for the heat absorption of refrigerant liquid carburation by evaporation, produce refrigerating capacity, the low-pressure steam of evaporation enters absorber 315;
Absorber 315, carries the low-pressure steam of coming from evaporimeter 314 for making to carry the bromize lithium concentrated solution of coming to absorb from generator 311, produces bromize lithium dilute solution;
Solution pump 317, for being pumped to generator 311 by the bromize lithium dilute solution in absorber 315; In pumping procedure, this bromize lithium dilute solution through described solution heat exchanger 316, liquation heat exchange dense with lithium bromide.
Because the pressure of generator and condenser is higher, and the pressure of absorber and evaporimeter is lower, therefore, preferably generator and condenser is arranged in a space, and absorber and evaporimeter are arranged in another space.Again due under being in high vacuum state when heat absorption type refrigeration unit works, therefore preferably its shelling machine is become columnar structured.High-pressure section is arranged in top, and low-pressure section is arranged in below, and centre solution tank separates.In addition, in the pipeline of generator to the dense liquation of absorber conveying lithium bromide, second throttle 318 can be installed.
As shown in Figure 3, described methanol-water reformation hydrogen production equipment 1 comprises methanol-water reservoir vessel 11, raw material conveying device 12, reformer 13 and membrane separation device 14; Described raw material conveying device 12 connects methanol-water reservoir vessel 11 and reformer 13 respectively by conveyance conduit, this raw material conveying device 12 by the methanol-water feedstock transportation in methanol-water reservoir vessel 11 to reformer 13; In conjunction with reference Fig. 4, described reformer 13 comprises heat exchanger 131, vaporizer, reformer chamber, separation chamber and exhaust emission device 131, and described membrane separation device 14 is arranged in separation chamber, and separation chamber is arranged at the top of reformer chamber; Described methanol-water raw material enters vaporizer vaporization in heat exchanger 131 after heat exchange; Methanol steam after vaporization and water vapour enter reformer chamber, reformer chamber is provided with catalyst, reformer chamber bottom and middle portion temperature are 300-420 DEG C, the temperature on described reformer chamber top is 400-570 DEG C, in reformer chamber, methyl alcohol and steam pass through catalyst under the pressure condition of 1-5M Pa, under the effect of catalyst, there is the transformationreation of methanol decomposition reaction and carbon monoxide, generate hydrogen and carbon dioxide, this is the gas solid catalytic reaction system of component more than, many reactions, and reactional equation is: (1) CH
3oH → CO+2H
2, (2) H
2o+CO → CO
2+ H
2, (3) CH
3oH+H
2o → CO
2+ 3H
2, the H that reforming reaction generates
2and CO
2; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350-570 DEG C, obtains hydrogen from the aerogenesis end of the membrane separation device 14 in separation chamber; The hydrogen partial that described reformer 13 is obtained is or/and residual air is run by burning maintenance reformer 13, and the waste gas produced after burning is expelled to described heat absorption type refrigeration unit 31 by exhaust emission device 132.Described membrane separation device 14 is the membrane separation device 14 at porous ceramic surface Vacuum Deposition palladium-silver, and film plating layer is palladium-silver, and the mass percent palladium of palladium-silver accounts for 75%-78%, and silver accounts for 22%-25%.
As Figure 4-Figure 6, described reformer 13 one end is provided with starting drive 4, and this starting drive 4 comprises cup 41, cup 41 is provided with raw material input channel 42, heating and gasifying pipeline 43, igniter 44 and temperature detection device 45; Described raw material input channel 42 can input first alcohol and water raw material, and raw material input channel 42 is connected with heating and gasifying pipeline 43, and first alcohol and water raw material enters after heating and gasifying pipeline 43 through raw material input channel 42, exports from the end of heating and gasifying pipeline 43; The position of described igniter 44 is corresponding with the end of heating and gasifying pipeline 43, for lighting a fire to the first alcohol and water raw material exported in heating and gasifying pipeline 43, first alcohol and water raw material is through igniter 44 ignition, combustion, can heat heating and gasifying pipeline 43, make the first alcohol and water material gasification in heating and gasifying pipeline 43 and strengthen rapidly combustion intensity, and then heating for reformer 13; Described temperature detection device 45 is for detecting the other temperature of heating and gasifying pipeline 43; After described reformer 13 starts hydrogen manufacturing, the hydrogen partial that reformer 13 is obtained is or/and residual air is run by burning maintenance reformer 13.Reformer 13 utilizes starting drive 4 to heat for reformer 13 just, just makes reformer 13 start, and then reforming reaction occurs, and start-up time can complete in 5 minutes, and very fast, after having started, starting drive 4 cuts out.
As Figure 4-Figure 6, described cup 41 comprises the liquid containing portion 412 above installation portion 411 and installation portion, described raw material input channel 42, heating and gasifying pipeline 43, igniter 44 and temperature detection device 45 are all installed on the installation portion 411 of cup, described liquid containing portion 412 can hold the first alcohol and water raw material exported from heating and gasifying pipeline 43 end, and described liquid containing portion 412 upper end is also provided with liquid Splashproof cover 413.After raw material input channel 42 inputs first alcohol and water raw material, when heating and gasifying pipeline 43 exports, unnecessary first alcohol and water raw material can be contained in the liquid containing portion 412 of cup, certainly, after first alcohol and water raw material burns rapidly, the first alcohol and water raw material in liquid containing portion 412 also can gasification, and combustion.Described liquid Splashproof cover 413 can prevent the first alcohol and water raw material splashes when gasification, and combustion in liquid containing portion 412.Described heating and gasifying pipeline 43 comprises straight-through pipeline section 431, pigtail 432 and upper arch pipeline section 433 successively, described first alcohol and water raw material can after straight-through pipeline section 431 rises to extreme higher position, decline through pigtail 432 spiral again, then export after upper arch pipeline section 433.Like this, when starting drive 4 is started working, first alcohol and water raw material enters heating and gasifying pipeline 43, and first alcohol and water raw material is under the effect of upper arch pipeline section 433, first alcohol and water raw material can ooze, so that igniter is lighted a fire from the end of upper arch pipeline section 433 in the mode of drippage; After lighting a fire successfully, because the entire length of pigtail 432 is long, heating surface area is large, and therefore, the first alcohol and water raw material in pigtail 432 can fully by thermal evaporation.
As shown in Figure 4, Figure 5, the bottom side of described cup 41 is provided with air intake cover plate 46, this air intake cover plate is provided with air channel 461, outside air can enter in reformer 13 through this air channel, the outside air entered from this air channel 461 can be starting drive 4 provides oxygen, also can be reformer 13 and oxygen is provided, for improving air inlet, fan (not shown) can be increased outside air channel 461; Described raw material input channel 42 is provided with magnetic valve, opens or closes to control raw material input channel 42.。Described igniter can adopt resistant to elevated temperatures igniter on market, such as electronic type pulse type ignitor etc.
The control method of the above-mentioned air-conditioning system based on methanol-water preparing hydrogen, generating power system, comprises the following steps:
A. methanol-water reformation hydrogen production equipment generation reformation hydrogen production reaction, the hydrogen that reformation hydrogen production reaction obtains flows to fuel cell, and in the process of reformation hydrogen production reaction, the heat delivery in the waste gas of discharge is to the heat absorption type refrigeration unit of thermoelectricity hybrid air-conditioning equipment;
B. fuel cell receives after hydrogen, the electrochemical reaction of hydrogen and oxygen occurs in fuel cell and produces electric energy, and the electric energy of generation is that the use electric-type air-conditioning unit of thermoelectricity hybrid air-conditioning equipment is powered;
C. the heat absorption type refrigeration unit of thermoelectricity hybrid air-conditioning equipment absorbs and freezes from after the heat in the waste gas of methanol-water reformation hydrogen production equipment discharge, freezes with the electric energy that electric-type air-conditioning unit consume fuel battery produces.
In above-mentioned steps c, the course of work of heat absorption type refrigeration unit comprises kind of refrigeration cycle step and solution circulation step, wherein:
Kind of refrigeration cycle step: be condensed into high pressure refrigerant liquid within the condenser from generator high pressure refrigerant vapor out, discharges the condenser heat medium that is cooled and takes away; The refrigerant liquid of high pressure refrigerant liquid under the throttling of first throttle valve is evaporating pressure, enter carburation by evaporation heat absorption in evaporimeter, produce refrigerating capacity, low-pressure steam is absorbed by absorber;
Solution circulation step: bromize lithium dilute solution in absorber absorbs evaporimeter and carries the low-pressure steam of coming and become bromize lithium concentrated solution; Absorption process makes lower pressure vapor refrigerant be converted into liquid, and absorption process is released the heat medium that is cooled and taken away; In absorber, bromize lithium concentrated solution improves pressure through solution pump, and is transported in generator, the heat in the waste gas utilizing methanol-water reformation hydrogen production equipment to discharge in generator and seethe with excitement concentrated, produces high pressure refrigerant vapor and the dense liquation of lithium bromide.
The above is only the utility model better embodiment, every above embodiment is done according to the technical solution of the utility model any trickle amendment, equivalent variations and modification, all belong in the scope of technical solutions of the utility model.
Claims (8)
1. based on the air-conditioning system of methanol-water preparing hydrogen, generating power system, it is characterized in that: comprise methanol-water reformation hydrogen production equipment, fuel cell and thermoelectricity hybrid air-conditioning equipment, wherein:
Methanol-water reformation hydrogen production equipment, react for first alcohol and water generation reformation hydrogen production, the hydrogen that reformation hydrogen production reaction obtains flows to fuel cell, and in the process of reformation hydrogen production reaction, the heat delivery in the waste gas of discharge is to the heat absorption type refrigeration unit of thermoelectricity hybrid air-conditioning equipment;
Fuel cell, produces electric energy for hydrogen and oxygen generation electrochemical reaction, and the electric energy of generation is that the use electric-type air-conditioning unit of thermoelectricity hybrid air-conditioning equipment is powered;
Thermoelectricity hybrid air-conditioning equipment, comprise heat absorption type refrigeration unit and use electric-type air-conditioning unit, heat absorption type refrigeration unit Absorbable rod methanol-water reformation hydrogen production equipment discharge waste gas in heat and freeze, with electric-type air-conditioning unit can consume fuel battery produce electric energy and freeze.
2. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 1, is characterized in that: described heat absorption type refrigeration unit comprises generator, condenser, first throttle valve, evaporimeter, absorber, solution heat exchanger and solution pump, wherein:
Generator, seethes with excitement concentrated for making the rare liquation of lithium bromide brought from absorber absorb the heat the waste gas of described methanol-water reformation hydrogen production equipment discharge, produces high pressure refrigerant vapor and the dense liquation of lithium bromide; High pressure refrigerant vapor flows to condenser, and the dense liquation of lithium bromide flows to absorber after solution heat exchanger heat exchange;
Condenser, is condensed into high pressure refrigerant liquid for high pressure refrigerant vapor, and the condenser heat discharged is taken away by cooling medium; The refrigerant liquid of high pressure refrigerant liquid under the throttling of first throttle valve is evaporating pressure, enters evaporimeter;
Evaporimeter, for the heat absorption of refrigerant liquid carburation by evaporation, produce refrigerating capacity, the low-pressure steam of evaporation enters absorber;
Absorber, carries the low-pressure steam of coming from evaporimeter for making to carry the bromize lithium concentrated solution of coming to absorb from generator, produces bromize lithium dilute solution;
Solution pump, for being pumped to generator by the bromize lithium dilute solution in absorber; In pumping procedure, this bromize lithium dilute solution through described solution heat exchanger, liquation heat exchange dense with lithium bromide.
3. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 1, is characterized in that: described methanol-water reformation hydrogen production equipment comprises methanol-water reservoir vessel, raw material conveying device, reformer and membrane separation device; Described raw material conveying device connects methanol-water reservoir vessel and reformer respectively by conveyance conduit, this raw material conveying device by the methanol-water feedstock transportation in methanol-water reservoir vessel to reformer; Described reformer comprises heat exchanger, vaporizer, reformer chamber, separation chamber and exhaust emission device, and described membrane separation device is arranged in separation chamber, and separation chamber is arranged at the top of reformer chamber; Described methanol-water raw material enters vaporizer vaporization in heat exchanger after heat exchange; Methanol steam after vaporization and water vapour enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300-420 DEG C, and the temperature on described reformer chamber top is 400-570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350-570 DEG C, obtains hydrogen from the aerogenesis end of the membrane separation device in separation chamber; The hydrogen partial that described reformer is obtained is or/and residual air maintains reformer operation by burning, and the waste gas produced after burning is expelled to described heat absorption type refrigeration unit by exhaust emission device.
4. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 3, it is characterized in that: described membrane separation device is the membrane separation device at porous ceramic surface Vacuum Deposition palladium-silver, film plating layer is palladium-silver, the mass percent palladium of palladium-silver accounts for 75%-78%, and silver accounts for 22%-25%.
5. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 3, it is characterized in that: described reformer one end is provided with starting drive, this starting drive comprises cup, cup is provided with raw material input channel, heating and gasifying pipeline, igniter and temperature detection device; Described raw material input channel can input first alcohol and water raw material, and raw material input channel is connected with heating and gasifying pipeline, and first alcohol and water raw material enters after heating and gasifying pipeline through raw material input channel, exports from the end of heating and gasifying pipeline; The position of described igniter is corresponding with the end of heating and gasifying pipeline, for lighting a fire to the first alcohol and water raw material exported in heating and gasifying pipeline, first alcohol and water raw material is through ignition device after-combustion, can heat heating and gasifying pipeline, make heating and gasifying ducted first alcohol and water material gasification and strengthen rapidly combustion intensity, and then being reformer heating; Described temperature detection device is for detecting the other temperature of heating and gasifying pipeline; After described reformer starts hydrogen manufacturing, the hydrogen partial that reformer is obtained is or/and residual air is run by burning maintenance reformer.
6. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 5, it is characterized in that: described cup comprises the liquid containing portion above installation portion and installation portion, described raw material input channel, heating and gasifying pipeline, igniter and temperature detection device are all installed on the installation portion of cup, described liquid containing portion can hold the first alcohol and water raw material exported from heating and gasifying pipe end, and described liquid containing portion upper end is also provided with liquid Splashproof cover.
7. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 5, it is characterized in that: described heating and gasifying pipeline comprises straight-through pipeline section, pigtail and upper arch pipeline section successively, described first alcohol and water raw material can after straight-through pipeline section rises to extreme higher position, decline through pigtail spiral again, then export after upper arch pipeline section.
8. the air-conditioning system based on methanol-water preparing hydrogen, generating power system according to claim 5, is characterized in that: the bottom side of described cup is provided with air intake cover plate, and this air intake cover plate is provided with air channel, and outside air can enter in reformer through this air channel; Described raw material input channel is provided with magnetic valve, opens or closes to control raw material input channel.
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| CN (1) | CN204404423U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104596001A (en) * | 2014-12-29 | 2015-05-06 | 广东合即得能源科技有限公司 | Air conditioning system based on methanol water hydrogen manufacturing and power generating system and control method thereof |
| WO2016070588A1 (en) * | 2014-11-07 | 2016-05-12 | 广东合即得能源科技有限公司 | Reformer for hydrogen production system utilizing methanol and water, hydrogen production system utilizing methanol and water and hydrogen production method |
| CN108793076A (en) * | 2018-07-26 | 2018-11-13 | 德州新动能铁塔发电有限公司 | A kind of reformer suitable for methanol-water hydrogen manufacturing |
| CN110867595A (en) * | 2018-08-28 | 2020-03-06 | 北京蓝吉新能源科技有限公司 | Fuel cell system and fuel cell automobile power system |
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2014
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016070588A1 (en) * | 2014-11-07 | 2016-05-12 | 广东合即得能源科技有限公司 | Reformer for hydrogen production system utilizing methanol and water, hydrogen production system utilizing methanol and water and hydrogen production method |
| CN104596001A (en) * | 2014-12-29 | 2015-05-06 | 广东合即得能源科技有限公司 | Air conditioning system based on methanol water hydrogen manufacturing and power generating system and control method thereof |
| CN104596001B (en) * | 2014-12-29 | 2019-03-19 | 广东合即得能源科技有限公司 | Air-conditioning system and its control method based on methanol-water preparing hydrogen, generating power system |
| CN108793076A (en) * | 2018-07-26 | 2018-11-13 | 德州新动能铁塔发电有限公司 | A kind of reformer suitable for methanol-water hydrogen manufacturing |
| CN110867595A (en) * | 2018-08-28 | 2020-03-06 | 北京蓝吉新能源科技有限公司 | Fuel cell system and fuel cell automobile power system |
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