CN107880959A - Chemical chain reforms methane system processed - Google Patents
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Abstract
本发明涉及化学链重整制甲烷领域,是一种高效的,清洁的化学链制甲烷系统。本发明主要由透氢膜反应发生器,化学链重整反应发生器,化学链燃烧反应发生器,换热器,液氧储存器组成,采用水煤气这一反应物质,将其通入透氢膜反应发生器,产生氢气,一氧化碳和部分水蒸气,将产生的氢气通入化学链燃烧反应发生器,将一氧化碳和部分水蒸气通入化学链重整反应发生器,经过一列的分离耦合过程完成反应,生成甲烷。本发明将空气反应器与燃料反应器等装置进行整合,以提高反应速率与燃料利用率及系统的经济性,具有很好的实际意义。
The invention relates to the field of methane production by chemical chain reforming, and is an efficient and clean chemical chain methane production system. The invention is mainly composed of a hydrogen permeable membrane reaction generator, a chemical chain reforming reaction generator, a chemical chain combustion reaction generator, a heat exchanger, and a liquid oxygen storage device. The reaction substance water gas is used to pass it into the hydrogen permeable membrane The reaction generator produces hydrogen, carbon monoxide and part of water vapor, passes the generated hydrogen into the chemical chain combustion reaction generator, passes carbon monoxide and part of water vapor into the chemical chain reforming reaction generator, and completes the reaction through a series of separation and coupling processes , producing methane. The invention integrates devices such as an air reactor and a fuel reactor to improve the reaction rate, fuel utilization rate and system economy, and has good practical significance.
Description
技术领域technical field
本发明涉及化学链重整制甲烷领域,是一种高效的,清洁的化学链制甲烷系统。The invention relates to the field of methane production by chemical chain reforming, and is an efficient and clean chemical chain methane production system.
背景技术Background technique
化学链燃烧是无火焰燃烧,其主要原理是将传统的燃料与氧气直接接触转变为借助载氧体与燃料和空气分表发生反应的过程,燃料不在与氧气直接接触,而是借助载氧体,将空气中的氧气由氧化物中的氧原子形式带入燃料中发生反应。Chemical chain combustion is flameless combustion. Its main principle is to transform the traditional direct contact between fuel and oxygen into the process of reacting with fuel and air with the help of oxygen carrier. The fuel is no longer in direct contact with oxygen, but with the help of oxygen carrier. , the oxygen in the air is brought into the fuel in the form of oxygen atoms in the oxide to react.
煤化学链制甲烷对清洁能源的转化利用有很大意义,传统的制甲烷过程中存在着物质的浪费,针对这一弊端,进行设计一种可循环使用的反应过程,通过循环利用,来减少物质的浪费。化学链是一种新型的环保高效的的能源转化及利用技术,这对煤化学链制甲烷提供了一种重要的途径,对改变传统的制甲烷,克服传统制作弊端有重要意义,为化石能源的清洁利用和高效利用提供了新的思路。并且通过这种方法可以优化终端能源结构。随着环保,如何高效利用能源已成为如今乃至将来要深刻讨论,并且解决的重要问题,所以对于研究一种化学链制甲烷的化学工艺符合时代发展规律,我们利用水煤气为原料来研究基于煤化学链制甲烷的工艺,并采取一种新的反应过程来实现。Coal chemical chain methane is of great significance to the conversion and utilization of clean energy. There is a waste of materials in the traditional methane production process. In view of this drawback, a recyclable reaction process is designed to reduce Material waste. Chemical chaining is a new type of environmentally friendly and efficient energy conversion and utilization technology. It provides an important way for coal chemical chaining methane production. It is of great significance to changing the traditional methane production and overcoming the disadvantages of traditional production. The clean utilization and efficient utilization provide new ideas. And through this method, the terminal energy structure can be optimized. With environmental protection, how to use energy efficiently has become an important issue that needs to be deeply discussed and solved today and even in the future. Therefore, the study of a chemical chain methane chemical process is in line with the development law of the times. We use water gas as raw material to study the chemical process based on coal chemistry. Chain methane process, and adopt a new reaction process to achieve.
发明内容Contents of the invention
通过水煤气变换膜制氢的反应来进行制氢气,水煤气通过膜将CO 和H2分离开来,将分离的氢气通入煤化学链反应进行合成CH4,剩余的CO 直接通入燃烧室,再将制成的CH4通入燃烧室进行燃烧,这样通过煤化学链反应可以得到纯度较好的CH4,避免了煤质进行直接燃烧产生的燃烧不充分,从而提升了燃烧效率,避免直接燃烧产生的不利因素。Hydrogen production is carried out through the reaction of water-gas shift membrane hydrogen production. Water gas is separated from CO and H 2 through the membrane, and the separated hydrogen is passed into the coal chemical chain reaction to synthesize CH 4 . The remaining CO is directly passed into the combustion chamber, and then Pass the produced CH 4 into the combustion chamber for combustion, so that CH 4 with good purity can be obtained through the coal chemical chain reaction, avoiding insufficient combustion caused by direct combustion of coal, thereby improving combustion efficiency and avoiding direct combustion unfavorable factors.
通过对透氢膜反应器中影响转化率的因素进行分析,采取装备甲基的SiO2膜来进行制取氢气。Through the analysis of the factors affecting the conversion rate in the hydrogen permeable membrane reactor, the SiO 2 membrane equipped with methyl groups is used to produce hydrogen.
本设备装置主要包括:透氢膜反应发生器,化学链重整反应发生器,化学链燃烧反应发生器,换热器,液氧储存器组成,采用水煤气这一反应物质,将其通入透氢膜反应发生器,产生氢气,一氧化碳和部分水蒸气,将产生的氢气通入化学链燃烧反应发生器,将一氧化碳和部分水蒸气通入化学链重整 反应发生器,经过一列的分离耦合过程生成甲烷等有机气体,生成的水蒸气经过化学链重整反应发生器生成氢气和部分氧离子,实现了水蒸气的循环使用,将生成的甲烷等有机可燃物经过换热器通入化学链燃烧反应发生器来进行能量转换。并将生成的富氧离子,经过氧载体,通入燃烧反应室,进行能量转移转化。系统原理示意图如图1所示。The device mainly includes: a hydrogen permeable membrane reaction generator, a chemical chain reforming reaction generator, a chemical chain combustion reaction generator, a heat exchanger, and a liquid oxygen storage tank. The hydrogen membrane reaction generator produces hydrogen, carbon monoxide and part of the water vapor, passes the generated hydrogen into the chemical chain combustion reaction generator, passes the carbon monoxide and part of the water vapor into the chemical chain reforming reaction generator, and passes through a series of separation and coupling processes Generate organic gases such as methane, and the generated water vapor passes through the chemical chain reforming reaction generator to generate hydrogen and some oxygen ions, which realizes the recycling of water vapor, and passes the generated organic combustibles such as methane through the heat exchanger into chemical chain combustion Reaction generators for energy conversion. And the generated oxygen-rich ions pass through the oxygen carrier and pass into the combustion reaction chamber for energy transfer and transformation. The schematic diagram of the system principle is shown in Figure 1.
(1)透氢膜反应发生器(1) Hydrogen permeable membrane reaction generator
通过水煤气变换膜制氢的反应来进行制氢气,水煤气通过膜将CO 和H2分离开来,将分离的氢气通入煤化学链反应进行合成CH4,剩余的CO 直接通入燃烧室,再将制成的 CH4通入燃烧室进行燃烧,这样通过煤化学链反应可以得到纯度较好的CH4,避免了煤质进行直接燃烧产生的燃烧不充分,从而提升了燃烧效率,避免直接燃烧产生的不利因素。Hydrogen is produced through the water-gas shift membrane hydrogen production reaction. Water gas separates CO and H 2 through the membrane, and passes the separated hydrogen into the coal chemical chain reaction to synthesize CH 4 . The remaining CO is directly passed into the combustion chamber, and then Pass the produced CH 4 into the combustion chamber for combustion, so that CH 4 with good purity can be obtained through the coal chemical chain reaction, avoiding insufficient combustion caused by direct combustion of coal, thereby improving combustion efficiency and avoiding direct combustion unfavorable factors.
(2)化学链重整反应发生器(2) Chemical chain reformation reaction generator
目的是提供一种成本低,能源转化率高,产氢效率高的基于化学链气化制甲烷及氢气的工艺。化学链制氢是一种新型高效制氢技术,该过程中氧载体携带的显热可提供气化反应所需要的热量,实现热量从放热反应器到吸热反应的热传递,同时借助于氧载体的循环,化学链制氢过程可实现氧从空气到水蒸气转移,同时将水分解为氢气和氧离子,CO与氢气反应合成甲烷和水,将CO加氢气化,和化学链催化制氢有机的耦合,可以实现煤质制取氢气和甲烷降低污染物的排放。The purpose is to provide a process for producing methane and hydrogen based on chemical loop gasification with low cost, high energy conversion rate and high hydrogen production efficiency. Chemical chain hydrogen production is a new type of high-efficiency hydrogen production technology. In this process, the sensible heat carried by the oxygen carrier can provide the heat required for the gasification reaction, and realize the heat transfer from the exothermic reactor to the endothermic reaction. The circulation of oxygen carriers, the process of chemical looping hydrogen production can realize the transfer of oxygen from air to water vapor, and at the same time decompose water into hydrogen and oxygen ions, the reaction of CO and hydrogen to synthesize methane and water, the hydrogenation and gasification of CO, and the catalytic production of chemical looping The coupling of hydrogen and organic can realize the production of hydrogen and methane from coal and reduce the emission of pollutants.
(3)化学链燃烧反应发生器(3) Chemical looping combustion reaction generator
减少温室气体CO2的排放量成为世界瞩目焦点,CO2的减排可通过提高能源的转化率,和利用效率来实现,如今化石燃料仍然将是主要的使用能源,通过常规的燃烧烟气中捕捉CO2困难很大,因此要从源头或过程中解决,本方案将采取从过程中通过化学链燃烧技术,来减少CO2排放,从而达到节能减排目的,化学链燃烧技术具有先天性捕获CO2的能力,而且还不需要额外的能量消耗,因此是实现高效清洁利用的一个新技术,具有广阔的发展前景。燃烧室中的化学链燃烧反应式为:The reduction of greenhouse gas CO 2 emissions has become the focus of the world. The reduction of CO 2 emissions can be achieved by improving the conversion rate and utilization efficiency of energy. Nowadays, fossil fuels will still be the main energy used. Through conventional combustion flue gas It is very difficult to capture CO 2 , so it must be solved from the source or the process. This plan will adopt the chemical looping combustion technology from the process to reduce CO 2 emissions, so as to achieve the purpose of energy saving and emission reduction. The chemical looping combustion technology has the inherent ability to capture CO 2 capacity, and does not require additional energy consumption, so it is a new technology to achieve efficient and clean utilization, with broad development prospects. The chemical looping combustion reaction in the combustion chamber is:
CH4(g)+H2O(g)→CO(g)+3H2(g) (2.1)CH 4 (g) + H 2 O (g) → CO (g) + 3H 2 (g) (2.1)
CO(g)+H2O(g)→CO2(g)+H2(g) (2.2)CO (g) + H 2 O (g) → CO 2 (g) + H 2 (g) (2.2)
(4)换热器(4) Heat exchanger
用来使热量从热流体传递到冷流体, 以满足规定的要求装置统称为换热器,按照换热器的工作状态,可将其分为,间壁式,混合式,蓄热式三类,最为广泛使用的为间壁式,间壁式换热器的主要形式套管式,管壳式换热器,交叉式换热器,我们采用间壁式换热器(如图2所示)来进行换热。The devices used to transfer heat from hot fluid to cold fluid to meet the specified requirements are collectively called heat exchangers. According to the working status of heat exchangers, they can be divided into three types: partition type, hybrid type, and heat storage type. The most widely used is the partition wall type, the main form of the partition wall heat exchanger is the casing type, the shell and tube heat exchanger, and the cross type heat exchanger. We use the partition wall heat exchanger (as shown in Figure 2) to exchange hot.
存储器的作用是用来储存氧气。The role of the memory is to store oxygen.
附图说明Description of drawings
图1为化学链重整制甲烷系统原理示意图,图2间壁式换热器二维示意图,图3化学链重整制甲烷系统原理反应图。Figure 1 is a schematic diagram of the principle of the chemical looping reforming methane system, Figure 2 is a two-dimensional schematic diagram of a partitioned wall heat exchanger, and Figure 3 is a schematic reaction diagram of the chemical looping reforming methane system.
具体实施方式Detailed ways
换热器的参数设计Parameter Design of Heat Exchanger
换热器参数设计为,设换热器进口水温20℃,出水水温设为60℃。换热器进口导热油为250℃,出口导热油温度为200℃;换热器水测的体积流量为12L/min。The parameters of the heat exchanger are designed as follows: the inlet water temperature of the heat exchanger is set at 20°C, and the outlet water temperature is set at 60°C. The heat transfer oil at the inlet of the heat exchanger is 250°C, and the temperature of the heat transfer oil at the outlet is 200°C; the volumetric flow rate measured by the water of the heat exchanger is 12L/min.
本设计计算采用平均温差法进行换热器的设计计算。In this design calculation, the average temperature difference method is used for the design calculation of the heat exchanger.
计算过程如下所示:The calculation process is as follows:
本设计采用壳侧1程、管侧4程管壳式换热器,换热管外径51mm,壁厚1mm。This design adopts a shell-and-tube heat exchanger with 1 pass on the shell side and 4 passes on the tube side. The outer diameter of the heat exchange tube is 51mm and the wall thickness is 1mm.
Ψ=0.98Ψ=0.98
查数据得:Check the data to get:
油侧表面传热系数h0=450w/m2gkOil side surface heat transfer coefficient h 0 =450w/m 2 gk
水侧表面传热系数hi=5850w/m2gkWater side surface heat transfer coefficient h i =5850w/m 2 gk
管内污垢热阻数值R0=0.000176m2gk/wThermal resistance value of fouling in the pipe R 0 =0.000176m 2 gk/w
管外污垢热阻数值Ri=0.000352m2gk/wThermal resistance value of fouling outside the tube R i =0.000352m 2 gk/w
实际设计取10%裕量:The actual design takes 10% margin:
A=A0×1.1=1.45m2 A=A 0 ×1.1=1.45m 2
优势分析advantage analysis
采取这种新型化学链反应,克服了传统燃烧反应和重整反应的弊端,减少污染物排放。化学链重整反应提高了反应物的转化率,转化为更清洁高效的产物,利于燃烧反应过程的进 行。化学链燃烧反应相对于传统的燃烧方式相比,其特有的燃烧方式及产生的污染是传统方 式不可企及的,具有污染小,产能高等特点。This new type of chemical chain reaction overcomes the drawbacks of traditional combustion and reforming reactions and reduces pollutant emissions. The chemical chain reforming reaction increases the conversion rate of the reactants, transforms them into cleaner and more efficient products, and facilitates the combustion reaction process. Compared with the traditional combustion method, the chemical looping combustion reaction has its unique combustion method and the pollution it produces is unattainable by the traditional method. It has the characteristics of low pollution and high production capacity.
对于采取透氢膜反应的创新点,其具有按要求分离特定的产物,转化速率高等特点,相对传统的转化方式具有方便简约,转化率高等特点,转化产物纯度较高,利于其他反应过程的进行,对于整个系统的反应转化过程具有一定的提升效果。For the innovative point of hydrogen permeable membrane reaction, it has the characteristics of separating specific products according to requirements and high conversion rate. Compared with the traditional conversion method, it is convenient and simple, with high conversion rate. The conversion product has high purity, which is beneficial to other reaction processes. , which has a certain improvement effect on the reaction transformation process of the whole system.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110951508A (en) * | 2019-12-16 | 2020-04-03 | 中国科学院山西煤炭化学研究所 | A calcium oxide-based coal chemical chain catalytic gasification device and process for methane production |
| CN115143510A (en) * | 2022-06-10 | 2022-10-04 | 北京市燃气集团有限责任公司 | Zero-carbon heating system |
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