CN206441813U - A kind of fuel cell for realizing first alcohol and water feed - Google Patents

A kind of fuel cell for realizing first alcohol and water feed Download PDF

Info

Publication number
CN206441813U
CN206441813U CN201621379783.XU CN201621379783U CN206441813U CN 206441813 U CN206441813 U CN 206441813U CN 201621379783 U CN201621379783 U CN 201621379783U CN 206441813 U CN206441813 U CN 206441813U
Authority
CN
China
Prior art keywords
evaporator
fuel cell
layer
plate
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201621379783.XU
Other languages
Chinese (zh)
Inventor
周明强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sino Hydrogen New Energy Technology Co Ltd
Original Assignee
Sino Hydrogen New Energy Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sino Hydrogen New Energy Technology Co Ltd filed Critical Sino Hydrogen New Energy Technology Co Ltd
Priority to CN201621379783.XU priority Critical patent/CN206441813U/en
Application granted granted Critical
Publication of CN206441813U publication Critical patent/CN206441813U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Abstract

The utility model discloses a kind of fuel cell for realizing first alcohol and water feed, including evaporator, the evaporator is connected with high-temperature fuel cell pile, the evaporator is provided with methanol charging aperture, water charging aperture and gas discharging opening, the base of evaporator is provided with heater, and inside is provided with multi-layer evaporation plate, every layer of evaporation plate and is provided with plate hole, the gas discharge mouthful is provided with copper zinc-base net, and the copper zinc-base net surface coats catalyst;The utility model has the advantage of:The Hydrogen Energy amount carried in methanol is not only converted into electric energy, while the Hydrogen Energy contained in water is converted into electric energy, the extraction and utilization of energy in water is realized;Heat effectiveness can be recycled without waste, improve hydrogen production efficiency and methanol conversion.

Description

A kind of fuel cell for realizing first alcohol and water feed
Technical field
The utility model is related to a kind of methanol fuel cell, specifically a kind of fuel electricity for realizing first alcohol and water feed Pond, belongs to methanol fuel cell field.
Background technology
Fuel cell technology is the generation technology for the chemical energy in fuel being converted directly into by electrochemical reaction electric energy. The energy conversion device that fuel cell is this efficiently, clean has obtained the most attention of national governments, army and research institution.By The characteristics of low-infrared radiation that has in fuel cell, low stain, low noise, fuel cell technology is shown extensively in military domain Wealthy application prospect.Traditional Proton Exchange Membrane Fuel Cells(PEMFC)Originated using hydrogen as energy, operating temperature is typically not Higher than 80 DEG C.But the technology is currently limited by hydrogen and is difficult to purify, stores, transporting and the characteristics of energy density is low, it is difficult to suitable Answer the requirement of high intensity military activity.It is different from above-mentioned traditional Proton Exchange Membrane Fuel Cells, methanol hydrogen fuel cell(MFC) Operation principle be by the way that hydrogen will be obtained after methanol recapitalization, then to be supplied directly to fuel cell to produce the technology of electric energy.By In using high temperature proton exchange film fuel cell technology, temperature of fuel cell operation is more than 100 DEG C, the catalysis in fuel cell Agent strengthens the anti-poisoning capability of carbon monoxide in hydrogen, thus the obtained hydrogen of methanol recapitalization can without any processing, Fuel cell is supplied directly to so as to obtain required electric energy, so as to avoid using the hydrogen solved needed for pure hydrogen fuel battery Purification, storage, transport and other a series of problems of gas.
Hydrogen production from methanol-steam reforming microreactor has many advantages, such as, but it still falls within technology primary stage, Ge Xiangji Art is not overripened, and methanol conversion is relatively low, and hydrogen output is not high, and fluid distrbution is uneven, the continuity that efficiency is utilized there is provided The problems such as stability of the energy, still hampers the progress and development of hydrogen production from methanol-steam reforming fuel cell.
Utility model content
The purpose of this utility model is, a kind of fuel cell for realizing first alcohol and water feed is devised, not only by methanol The Hydrogen Energy amount of middle carrying is converted to electric energy, while the Hydrogen Energy contained in water is converted into electric energy, realize in water the extraction of energy with Utilize;Heat effectiveness can be recycled without waste, improve hydrogen production efficiency and methanol conversion.
The technical solution of the utility model is:
A kind of fuel cell for realizing first alcohol and water feed, including evaporator, the evaporator and high-temperature fuel cell electricity Heap is connected, and the evaporator is provided with methanol charging aperture, water charging aperture and gas discharging opening, and the base of evaporator is filled provided with heating Put, inside is provided with multi-layer evaporation plate, every layer of evaporation plate and is provided with plate hole, and the first alcohol and water mixed vapour after evaporation is by steaming The plate hole of hair plate enters is provided with copper zinc-base net, the copper zinc-base net surface with high-temperature fuel cell pile, the gas discharge mouthful Catalyst is coated, processing generation H can be carried out to the mixed vapour of first alcohol and water2、CO2, trace amounts of CO, vapor, improve hydrogen manufacturing Efficiency and methanol conversion.
Further, the high-temperature fuel cell pile is made up of multiple monocell plates, and the monocell plate is 7 Rotating fields From left to right be followed successively by positive plate, anode diffusion layer, anode catalyst layer, PEM, cathode catalysis layer, cathode diffusion layer, Minus plate, the monocell of varying number is pressed into the pile of different capacity.The fuel battery temperature is controlled at 150-200 degrees Celsius Between, belong to high-temperature fuel cell.Hydrogen enters anode diffusion layer via polar plate flow field, through catalytic reaction ionization generation H+And electricity Son, H+Cell cathode side is transferred to through PEM, the electronics of generation delivers to negative electrode by conductive materials through external circuit;With this Meanwhile, oxygen enters cathode diffusion layer via minus plate flow field, is generated in cathode catalysis layer with anode and is transferred to battery the moon The H of pole side+And electron reaction generation water.The heat produced in high temperature pile course of reaction, leads back to evaporator for methanol water evaporation Energy is provided.
The utility model has the advantage of:The Hydrogen Energy amount carried in methanol is not only converted into electric energy, while will contain in water Some Hydrogen Energies are converted into electric energy, realize the extraction and utilization of energy in water;Heat effectiveness can be recycled without waste, Improve hydrogen production efficiency and methanol conversion.
The utility model is described in further detail with reference to the accompanying drawings and examples.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment
Preferred embodiment of the present utility model is illustrated below, it will be appreciated that preferred embodiment described herein The utility model is merely to illustrate and explained, is not used to limit the utility model.
Embodiment 1
As shown in figure 1, a kind of fuel cell for realizing first alcohol and water feed, including evaporator, the evaporator and high temperature Fuel cell pile is connected, and the evaporator is provided with methanol charging aperture, water charging aperture and gas discharging opening, the base of evaporator Provided with heater, inside is provided with multi-layer evaporation plate, every layer of evaporation plate and is provided with plate hole, the first alcohol and water mixing after evaporation Steam is entered by the plate hole of evaporation plate is provided with copper zinc-base net, the copper with high-temperature fuel cell pile, the gas discharge mouthful Zinc-base net surface coats catalyst, and processing generation H can be carried out to the mixed vapour of first alcohol and water2、CO2, trace amounts of CO, vapor, Improve hydrogen production efficiency and methanol conversion.
Further, the high-temperature fuel cell pile is made up of multiple monocell plates, and the monocell plate is 7 Rotating fields From left to right be followed successively by positive plate, anode diffusion layer, anode catalyst layer, PEM, cathode catalysis layer, cathode diffusion layer, Minus plate, the monocell of varying number is pressed into the pile of different capacity.The fuel battery temperature is controlled at 150-200 degrees Celsius Between, belong to high-temperature fuel cell.Hydrogen enters anode diffusion layer via polar plate flow field, through catalytic reaction ionization generation H+And electricity Son, H+Cell cathode side is transferred to through PEM, the electronics of generation delivers to negative electrode by conductive materials through external circuit;With this Meanwhile, oxygen enters cathode diffusion layer via minus plate flow field, is generated in cathode catalysis layer with anode and is transferred to battery the moon The H of pole side+And electron reaction generation water.The heat produced in high temperature pile course of reaction, leads back to evaporator for methanol water evaporation Energy is provided.

Claims (2)

1. a kind of fuel cell for realizing first alcohol and water feed, it is characterised in that:Including evaporator, the evaporator fires with high temperature Expect that battery pile is connected, the evaporator is provided with methanol charging aperture, water charging aperture and gas discharging opening, the base of evaporator is set There is heater, inside, which is provided with multi-layer evaporation plate, every layer of evaporation plate, is provided with plate hole, and the gas discharge mouthful is provided with copper zinc Base net, the copper zinc-base net surface coats catalyst.
2. a kind of fuel cell for realizing first alcohol and water feed according to claim 1, it is characterised in that:The high temperature combustion Material battery pile is made up of multiple monocell plates, and the monocell plate is that 7 Rotating fields are from left to right followed successively by positive plate, anode expansion Dissipate layer, anode catalyst layer, PEM, cathode catalysis layer, cathode diffusion layer, minus plate.
CN201621379783.XU 2016-12-15 2016-12-15 A kind of fuel cell for realizing first alcohol and water feed Active CN206441813U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621379783.XU CN206441813U (en) 2016-12-15 2016-12-15 A kind of fuel cell for realizing first alcohol and water feed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621379783.XU CN206441813U (en) 2016-12-15 2016-12-15 A kind of fuel cell for realizing first alcohol and water feed

Publications (1)

Publication Number Publication Date
CN206441813U true CN206441813U (en) 2017-08-25

Family

ID=59646867

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621379783.XU Active CN206441813U (en) 2016-12-15 2016-12-15 A kind of fuel cell for realizing first alcohol and water feed

Country Status (1)

Country Link
CN (1) CN206441813U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109830721A (en) * 2019-01-21 2019-05-31 西安交通大学 Product drives feed separation transmission direct methanol fuel cell and its working method
CN112397751A (en) * 2020-11-04 2021-02-23 江苏科技大学 Methanol reforming solid oxide fuel cell system and working method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109830721A (en) * 2019-01-21 2019-05-31 西安交通大学 Product drives feed separation transmission direct methanol fuel cell and its working method
CN112397751A (en) * 2020-11-04 2021-02-23 江苏科技大学 Methanol reforming solid oxide fuel cell system and working method
CN112397751B (en) * 2020-11-04 2022-03-08 江苏科技大学 Methanol reforming solid oxide fuel cell system and working method

Similar Documents

Publication Publication Date Title
CN108206289B (en) Fuel cell prepared based on methanol and water reforming
CN206225464U (en) A kind of methanol fuel cell assembly of porous metal fiber plate
JP2007538379A5 (en)
CA2694153A1 (en) Steam reformation fuel cell with waste heat cogeneration turbine heat to energy pyroelectric crystals and/or thermo-coupling any and all waste heat to energy technologies and/or new macro-micros fuel cell power plant design
US8603694B2 (en) Method for operating fuel cells for systems that are restricted by exposure to thermal stress and fuel cell stack for carrying out said method
JP4956946B2 (en) Fuel cell
CN206441814U (en) One kind is based on polymer bipolar end plates composite methanol fuel cell unit
CN206441813U (en) A kind of fuel cell for realizing first alcohol and water feed
Shi et al. Effect of operating parameters on the performance of thermally regenerative ammonia-based battery for low-temperature waste heat recovery
CN100550500C (en) A kind of fuel battery
CN206789625U (en) A kind of hydrogen fuel cell pile based on bipolar plates
CN206340609U (en) A kind of methanol fuel cell utilized based on reformation and the integrated efficiency of pile
CN109876751B (en) Plasma reactor and application thereof
JP2007005134A (en) Steam generator and fuel cell
JP2007005133A (en) Steam generator and fuel cell
CN111063912B (en) Vein bionic pressure-permeation type three-in-one bipolar plate and working method thereof
JP2003308869A (en) Fuel cell
Dong et al. A membrane-less molten hydroxide direct carbon fuel cell with fuel continuously supplied at low temperatures: A modeling and experimental study
Farooque et al. Carbonate fuel cell technology and materials
JP2010086893A (en) Stack structure of fuel cell
CN106299422B (en) A kind of electrochemistry tail gas recycling device
Chaurasia et al. Performance study of power density in PEMFC for power generation from solar energy
CN206301882U (en) A kind of micro fuel cell apparatus
CN112993315A (en) Heat coupling methanol reforming hydrogen production fuel cell system
CN113346092B (en) Fluidized bed electrode solid oxide fuel cell device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant