With the rapid development of economy, the demand for oil resources is increasing day by day, and the import of a large amount of oil will affect the energy security. Therefore, the development of alternative fuels and the development of clean energy have become an important choice of energy strategy. In recent years, dimethyl ether has become a hot topic of petroleum substitution products and new two energy sources, which has aroused great concern and attention of governments and experts in Europe, America, and Japan. The development of the dimethyl ether economic system is of great strategic significance for economic development, environmental protection and ecological balance   .
The generation of hydrogen from fossil fuels such as alcohols, ethers and hydrocarbons for fuel cell power generation is considered to be one of the most realistic hydrogen source solutions in the near and medium term. However, these substances have some defects in the process of reforming hydrogen production, such as, hydrogen production by methane reforming requires a higher temperature, while additional hydrogen gasification equipment is needed during the process of reforming methanol to hydrogen, which increases the operation cost, and methanol has certain toxicity  . When a small amount of hydrogen is added to the dimethyl ether engine, the advantages are as follows: 1) high combustion efficiency; 2) reduce emissions of NOx and soot in automobile exhaust   . DME is an environmentally friendly clean and safe liquid fuel. It is easy to compress into liquid, and DME has the advantages of high energy density, non-toxicity, easy availability, safe handling and storage    .
2. Method and Mechanism of Hydrogen Production from DME
2.1. Method of Hydrogen Production from DME
Two ways of hydrogen production by reforming of dimethyl ether are as follows: DME steam reforming (DME SR), DME partial oxidation reforming of hydrogen (POX), DME autothermal reforming (DME ATR), and technology of DME plasma  .
Steam reforming of DME process involves following four main reactions  :
1) Water-gas shift:
2) DME hydrolysis:
3) Steam reforming of methanol:
4) Methanol decomposition:
SR has been widely used in different industrial production of hydrogen, however, the reaction is endothermic, this process requires high external heat source. Francis A. Elewuwa et al. presents a computational parametric analysis of DME steam reforming in a large scale Circulating Fluidized Bed (CFB) reactor   . Feng et al. has presented a kinetic rate of total combustion of DME based on copper-based catalyst  .
Partial oxidation of DME reaction:
Partial oxidation process is an exothermic process with quick start and less complex, however, high carbon monoxide concentration produced in the reaction will poison the catalyst of the fuel cell.
Autothermal reforming of DME reaction:
The autothermal reforming of dimethyl ether is the coupling of the two reforming methods. By this method, the concentration of hydrogen in high concentration products is avoided, and no external heating is needed. The purpose of this research is to supply hydrogen for large fuel cell vehicle. Derek Creaser et al. developed a global kinetic model for the autothermal reforming of dimethyl ether (DME) over a Pd-Zn/Al2O3 catalyst on a cordierite monolith  . M. H. Akbari et al. presented a numerical investigation of catalytic autothermal reforming of methane in a surface microreactor  .
The principle of plasma hydrogen production is radical plasma rich mixture using hydrocarbon fuel and air by arc discharge generated in the region, caused by partial oxidation reaction to produce hydrogen rich gas, hydrogen is considered a high efficiency and low cost. The method is similar to the traditional method of hydrogen production, the difference is that the active substances that excite the chemical reactions are different.
2.2. Mechanism of Hydrogen Production from DME
Hydrogen production from steam reforming of DEM is a continuous reaction: the first step is DME hydrolysis into methanol on an acidic catalyst; the second step is to produce hydrogen in the methanol reforming of the metal catalyst. The DME hydration of methanol is a thermodynamic equilibrium limit, but immediately produced methanol steam reforming reaction. In addition to the above 2 reactions, water gas shift reaction (WGSR) may occur   .
The mechanism of hydrogen production by DME steam reforming should be based on the mechanism of two methyl ether hydration and methanol steam reforming, and the mechanism of DME synthesis, methanol dehydration and water gas shift reaction should be combined. Study on the DME steam reforming mechanism and kinetics of hydrogen production, establish reasonable rate model, the DME conversion and hydrogen yield forecast, provide for the design of the reformer dynamic information and dynamic data needed is very important, which can accelerate the fuel cell vehicle commercialization process.
Kinetic modeling of catalytic steam reforming of DME is as following:
1) DME hydrolysis into methanol 
2) Methanol steam reforming 
3) Methanol decomposition 
4) WGS reaction 
2.3. Influence of Operating Parameters
The main factors affecting the reaction rate and chemical balance of hydrogen production by steam reforming of two methyl ether are as follows:
1) Temperature. Because the reaction of hydrogen production by steam reforming of DME is endothermic, the conversion rate increases with the increase of temperature, but the concentration of CO increases. Therefore, in order to save energy and reduce the content of CO in the products, a low reaction temperature should be adopted to match the fuel cell.
2) Pressure. As the reaction is an increase in volume, the conversion decreases as the pressure increases. If the membrane reactor is adopted, the reaction system should have a certain pressure. Feed ratio of water and DME. With the increase of water quantity, the conversion of DME can be promoted.
3. Catalyst for Reforming of DME
There are very strict restrictions on the content of hydrogen rich gas supplied in CO PEMFC, and electric vehicles for fuel cell power supply requirements of compact structure and small device, so to ensure the high hydrogen yield at the same time, should reduce the content of CO in hydrogen rich gas. Therefore, the search for catalysts with low temperature, high activity and high selectivity is the focus of the study on the two methyl ether reforming, and also a key technology for hydrogen production on board.
3.1. Catalyst for Steam Reforming of DME
DME steam reforming catalyst active component generally consists of two parts: solid acid catalyst and metal or metal oxide, wherein the solid acid catalyst to help DME hydrolysis reaction, and metal or metal oxide contributes to the methanol reforming reaction. The study shows that the hydrolysis rate of DME is the speed control step of the whole reforming process. Therefore, scholars at home and abroad have done a lot of research on the effect of acid carrier in the process of hydrolysis of DME. According to the micro reversibility principle of chemical reaction, a solid acid catalyst with good activity in the process of methanol dehydration to produce DME is proposed. Feng et al.  developed a one-dimensional isotherm plug flow model to simulate DME-SR in a fixed bed reactor with bifunctional catalyst CuO/ZnO/Al2O3/+ZSM-5. Other catalysts, such as mechanically mixed HPA/Al2O3 acidic catalyst and Cu/SiO2 metallic catalyst, have been tested experimentally in a fixed bed reactor and reported to achieve near 100% DME conversion at 290˚C  .
3.2. Catalyst for Autothermal Reforming of DME
Autothermal reforming of DME is the coupling of the two DME hydrogen production methods, and has the advantages of two reactions, namely, steam reforming and partial oxidation. Derek Creaser 8 et al. proposed a global kinetic model for the autothermal reforming of dimethyl ether (DME) over a Pd-Zn/Al2O3 catalyst  . M. Nilsson  et al. has tested the performance of the catalysts in a small-scale reactor, using cordierite monoliths as substrate. The catalysts exhibited high activity and generated hydrogen-rich product gases with CO concentrations below 5 vol.% in the temperature range between 350˚C and 450˚C (at O2:DME = 0.7, H2O:DME = 2.5, and GHSV = 15,000 h−1).
3.3. Catalyst for Partial Oxidation Reforming of DME
Hydrogen production by partial oxidation reforming of two - methyl ether is an exothermic reaction, and it is easy to form a “hot spot” in the reactor, resulting in the decrease of the effective utilization coefficient of the catalyst. Zhang  et al. has proposed that H2 yield of more than 90% was obtained with little methane production over Pt/Al2O3 and Ni-MgO combined catalysts. Ni-MgO was active for the reforming of DME as well as for the reforming of CH4, which formed through a homogeneous reaction between DME and oxygen. Chen  et al. presents results of DME partial oxidation over a 1.5 wt% Pt/Ce0.4Zr0.6O2 catalyst under the condition of gas hourly space velocity (GHSV) of 15,000 - 60,000 ml/(g・h), molar ratio of O2/DME of 0.5 and 500˚C - 700˚C, and this temperature range was also the operation temperature range for intermediate temperature SOFC.
For catalysts, in addition to activity and selectivity, their lifetime is also an important indicator of the performance of the catalyst. There are many factors that affect the life, and the deposition of reaction by-products, such as carbon deposition, is the main problem that leads to deactivation of catalysts and limits the industrial application of DME hydrogen production technology.
The commercialization of fuel cell vehicle is not only restricted by the development level of fuel cell itself, but also affected by the fuel supply facilities and fuel storage. An ideal hydrogen fuel vehicle with its high energy density, low carbon content and convenient transportation and storage and other advantages, and the hydrogen production unit size are advised, and can be made into a mobile device to satisfy the requirements of different users of hydrogen source. From the overall situation, the current study on DME reforming hydrogen production catalyst has just started, the future development of DME catalysts with high performance, to carry out research on DME catalytic reaction mechanism and reaction kinetics, the development of membrane technology, has important significance to improve the level of hydrogen storage. Hydrogen fuel is the most promising fuel cell electric vehicle. DME hydrogen mixing combustion can improve engine efficiency and reduce emissions. Therefore, in order to realize the convenient and safe hydrogen production on the vehicle, a variety of hydrogen production technologies must be studied, including steam reforming, partial oxidation, autothermal reforming and plasma weighting.
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