首页> 外文OA文献 >Business Model and Replication Study of BIG HIT
【2h】

Business Model and Replication Study of BIG HIT

机译:BIG HIT的商业模式与复制研究

摘要

Due to concerns about climate change, negative environmental impacts of some fuels, and the decline in the availability of fossil fuels, renewable energy technologies are growing rapidly and becoming mature. Such technologies can provide a major share of electricity supply demand globally. However, as their market share grows, concerns about potential impacts on the stability and operation of the electricity grid, as well as economic impacts due to grid upgrading requirements, may create barriers to their future expansion, due to renewable electricity’s intermittent productions and variability. ‘Green hydrogen’ can be seen as one of the solutions to integrate high penetrations of renewables in the energy system, using both the electricity and gas networks. At present, the ‘green hydrogen’ market is small and prices are high. However, costs can be driven down by upscaling the production of equipment to mass production; supply chain optimisation, and there is also still room for technology improvement. Now is the time to prepare for the integration of significant quantities of ‘green hydrogen’ into the energy system and gain experience from large-scale demonstration of relevant hydrogen concepts.The BIG HIT project is creating a replicable hydrogen territory in Orkney (An island archipelago six miles offshore from North of Mainland Scotland.) by implementing a fully integrated model of hydrogen production, storage, distribution of the hydrogen across Orkney and utilised for mobility, heat and power. The BIG HIT project will use otherwise curtailed electricity from one wind turbine on Shapinsay and one wind turbine and a tidal test sites on Eday, and use 1.5 MW of Polymer Electrolyte Membrane (PEM) electrolyser to convert it into ~50 t pa of hydrogen. This will be used to provide heat to local public buildings. The excess hydrogen will be transported by ferry in hydrogen tube trailers to the Orkney islands largest town, Kirkwall, where it will be used to fuel a 75 kW fuel cell stack (which will provide heat and power to ferries when docked); and the remaining hydrogen will be used at a refuelling station to fuel a fleet of up to 10 electric-hydrogen range extended vans.The present business model report includes a financial analysis of the demonstration project and should provide an early warning if there is anything that would require the project to be altered (for example, to negotiate negative priced input electricity). By gathering and critically examining inputs from project partners and equipment suppliers: electrolyser (ITM power), tube trailer (Calvera), catalytic hydrogen (H2) boilers (Giacomini), compressor (Hofer), fuel cell stack (Arcola Energy), Hydrogen Fuel Cell (H2 FC) van (SymbioFCell) and other stakeholders, the business model is developed within the 1st year of the project.The cost analysis of this project considers the life cycle of hydrogen starting from the hydrogen production, transportation, and consumption. The cost includes the fixed cost for equipment and infrastructure investment and operation cost of electricity and water consumption. The functional unit is 1 kg hydrogen produced and consumed. The data collected from the project patterns and suppliers. The current analysis is based on the estimation of hydrogen production and consumption on both Shapinsay and Eday. Another objective of this report is replicability of the concept for follower territories of BIG HIT. So the cost of a replicated BIG HIT concept in the 5th year after starting BIG HIT is modelled based on the assumed capital cost reductions. Capital costs will be driven down through mass production or supply chain optimisation, and also by the technology development.Under the two different time frames (present expectations and replication after 5 years of BIG HIT), five different scenarios are built to analyse the cost. In the first scenario S1 (current situation with limited use of curtailed energy) and the second scenario S2 (full utilisation of curtailed energy), the electrolysers on Eday and Shapinsay are directly connected to wind turbines and tidal test site. The electricity supply for the electrolyser is only from otherwise curtailed electricity. In the third scenario S3 (full utilization of electrolysis capacity and the consumed electricity from curtailed electricity), the fourth scenario S4 (full capacity of electrolyser and electricity from both curtailed electricity and power grid), and the fifth scenario S5 (full capacity of electrolyser and the consumed electricity from power grid), the electrolysers are connected to both the wind turbines and tidal test sites and the electricity grid. In the scenarios S3, S4, and S5, it is assumed that the electrolysers can operate at full capacity and run continuously at 24 hours per day. Further it is assumed, that there is a consistent demand of ‘green hydrogen’ on the market. The difference between the otherwise curtailed electricity and grid electricity is the price. The otherwise curtailed electricity would generate an income from Feed in Tariff (FiT), which also lead to the motivation for the hydrogen producer by using the curtailed electricity. In the current BIG HIT situation (S1) the cost of hydrogen production is calculated to be 9.87 £/kg on Shapinsay and 5.17 £/kg on Eday. Two reasons cause the cost of hydrogen production to be lower on Eday than on Shapinsay. Firstly, hydrogen produced on Eday has the priority to be transported to the fuel cell in Kirkwall, which means there would be no hydrogen unconsumed on Eday. Secondly, the cost of electricity consumed by electrolyser on Eday is less than that on Shapinsay. The difference is made by Eday Renewable Energy ltd. (ERE) sharing their FiT with the project Surf ‘n’ Turf (SnT) and the BIG HIT project where Shapinsay Renewables Limited, a child company of Shapinsay Development Trust (SDT) does not have the same agreement for the BIG HIT project by now. If the curtailed electricity from the wind turbines could be fully absorbed and the produced hydrogen would be transported and consumed consistently, the cost of producing hydrogen will decrease to 6.92 £/kg on Shapinsay if the agreement of electricity cost is same with that in S1. If the electricity cost is based on FiT, the cost of producing hydrogen will decrease to 2.52 £/kg presented in S2. With increasing of the running capacity, the cost of producing hydrogen can decrease to -2.33 £/kg with FiT support. In the replicated BIT HIT scenarios, the costs of producing hydrogen on Shapinsay are 9.02 £/kg and 2.00 £/kg in S1 and S2, respectively. If there would be no FiT for renewable electricity production in the future, the cost of hydrogen production will be 12.38 £/kg and 13.21 £/kg on Shapinsay and Eday, respectively (S5). The major cost comes from the cost of the electricity consumed from power grid. In the replicated BIT HIT project scenarios, the cost can decrease to 12.34 £/kg and 13.12 £/kg on Shapinsay and on Eday. This difference between from Shapinsay and Eday is due to the different capacity of electrolyser, 1 MW and 0.5 MW respectively.The utilizations of hydrogen considered in this demonstration project are heat, electricity, and mobility. The replaced conventional energy sources are oil for heat, electricity from power grid, and diesel for mobility. The functional unit is defined as 1 kg hydrogen consumed. The costs of conventional fuels are obtained from the market price. The amounts of conventional fuels are calculated based on the same amounts of energy obtained from 1 kg hydrogen. The considered system boundary includes the hydrogen production process, hydrogen transportation, and hydrogen consumption. At each stage, the data has been collected from the project partners and equipment suppliers/manufacturers. The cost of hydrogen is calculated through the life cycle of hydrogen production and consumption. The suggested price of hydrogen in order to offer a cost-competitive solution is estimated. If the purpose is to supply heat (by boiler), the competitive hydrogen price is estimated to be between 1.22 £/kg and 1.28 £/kg without or with considering CO2 emission cost. If the purpose is to provide electricity and heat through a fuel cell unit, the competitive hydrogen price is between 1.48 £/kg and 2.97 £/kg without or with considering CO2 emission cost. If hydrogen is used as fuel for hydrogen fuel cell vehicles, the competitive price level of hydrogen is estimated to be 8.85 £/kg and 8.46 £/kg without or with considering CO2 emission cost.By the comparison of the total costs for a certain heat, power or mobility service, between hydrogen technologies and conventional technologies, it is concluded that mobility is the application where hydrogen is closest to offer a cost-attractive proposition to the conventional technology, i.e. mobility using diesel as energy source. In the present scenarios, hydrogen is not close to being cost-competitive for neither heat purposes nor power purposes.
机译:由于对气候变化的担忧,某些燃料对环境的负面影响以及化石燃料的可用性下降,可再生能源技术正在迅速发展并日趋成熟。此类技术可以在全球范围内提供大部分的电力供应需求。但是,随着市场份额的增长,由于可再生电力的间歇性生产和可变性,对电网稳定性和运行的潜在影响以及电网升级要求带来的经济影响的担忧可能会为其未来的扩张创造障碍。可以将“绿色氢”视为使用电力和天然气网络将高渗透率的可再生能源整合到能源系统中的解决方案之一。目前,“绿色氢”市场很小,价格也很高。但是,可以通过将设备的生产规模扩大到批量生产来降低成本。供应链的优化,而且技术还有改进的空间。现在是时候准备将大量的``绿色氢''整合到能源系统中,并从大规模演示相关氢概念中获得经验.BIG HIT项目正在奥克尼岛(一个岛屿群岛)创建可复制的氢域(距苏格兰大陆北部以北约六英里)。通过实施完全整合的制氢模型,在整个奥克尼群岛生产,储存和分配氢气,并将其用于交通,热力和动力。 BIG HIT项目将使用Shapinsay的一台风力涡轮机以及Eday的一台风力涡轮机和潮汐试验场所减少的电力,并使用1.5 MW的聚合物电解质膜(PEM)电解器将其转化为约50 t pa的氢气。这将用于为当地的公共建筑供热。多余的氢气将通过渡轮在氢气管拖车中运输到奥克尼群岛最大的城镇柯克沃尔,在那里将为75 kW的燃料电池堆提供燃料(在停靠时将为渡轮提供热量和电力);剩余的氢气将在加油站中使用,以为最多10辆氢动力扩展加长型货车加油。本商业模式报告包括对示范项目的财务分析,如果有任何发现,应提供预警。将需要更改项目(例如,协商负价输入电)。通过收集并严格审查来自项目合作伙伴和设备供应商的投入:电解器(ITM电源),管式拖车(Calvera),催化氢(H2)锅炉(Giacomini),压缩机(Hofer),燃料电池堆(Arcola Energy),氢燃料Cell(H2 FC)货车(SymbioFCell)和其他利益相关者,在项目的第一年内就开发了商业模型。该项目的成本分析从氢的生产,运输和消耗开始考虑氢的生命周期。该成本包括设备和基础设施投资的固定成本以及电力和水消耗的运营成本。功能单位是产生和消耗1公斤氢气。从项目模式和供应商收集的数据。当前的分析基于对Shapinsay和Eday的氢气生产和消耗的估计。该报告的另一个目标是对BIG HIT追随者地区的概念具有可复制性。因此,在开始BIG HIT后的第5年中,将使用复制的BIG HIT概念的成本是基于假定的资本成本减少进行建模的。资本成本将通过批量生产或供应链优化以及技术开发来降低。在两个不同的时间框架内(目前的期望值和BIG HIT的5年后的复制),构建了五个不同的方案来分析成本。在第一种情况S1(当前仅使用有限的缩减能源的情况)和第二种情况S2(已完全使用缩减的能源)中,Eday和Shapinsay的电解槽直接连接到风力涡轮机和潮汐试验场。电解槽的电力供应仅来自减少的电力。在第三种情况S3(电解能力的充分利用和电力的削减所消耗的电量)中,第四种情况S4(电解器的全部产能以及削减的电力和电网产生的电力)和第五种情况S5(电解器的全部产能)以及从电网消耗的电能),则将电解槽同时连接到风力涡轮机和潮汐测试站点以及电网。在方案S3,S4和S5中,假定电解槽可以满负荷运行,并且每天24小时连续运行。进一步假设,市场上一直有对“绿色氢”的需求。否则减少的电力与电网电力之间的差额就是价格。否则,减少的电力将通过上网电价(FiT)产生收入,这也将导致通过使用减少的电力来激励制氢者。在当前的大HIT情况下(S1),Shapinsay的制氢成本为9.87£/ kg,Eday的制氢成本为5.17£/ kg。有两个原因导致Eday的制氢成本比Shapinsay低。首先,在Eday产生的氢气优先被运输到Kirkwall的燃料电池,这意味着在Eday不会有氢气被消耗。其次,Eday电解槽的耗电成本比Shapinsay的低。区别在于Eday Renewable Energy ltd。 (ERE)与Surf'n'Turf(SnT)项目和BIG HIT项目共享其FiT,而Shapinsay Development Trust(SDT)的子公司Shapinsay Renewables Limited到目前为止尚未就BIG HIT项目达成相同的协议。如果来自风力涡轮机的减少的电力能够被充分吸收,并且所产生的氢能够被一致地运输和消耗,那么如果用电协议与S1中的协议相同,则在Shapinsay上,产生氢的成本将降至6.92£/ kg。如果电力成本基于FiT,则制氢成本将降至S2中显示的2.52£/ kg。随着运行能力的提高,在FiT的支持下,制氢成本可降低至-2.33£/ kg。在重复的BIT HIT情景中,在Shapinsay上生产氢气的成本分别为S1和S2为9.02£/ kg和2.00£/ kg。如果将来没有针对可再生电力生产的上网电价补贴,那么在夏平赛和伊代,制氢成本将分别为12.38英镑/千克和13.21英镑/千克(S5)。主要成本来自电网消耗的电力成本。在重复的BIT HIT项目方案中,Shapinsay和Eday的成本可以降低到12.34£/ kg和13.12£/ kg。与Shapinsay和Eday之间的差异是由于电解槽的容量不同(分别为1 MW和0.5 MW)。在此示范项目中考虑的氢利用为热,电和迁移率。替代的常规能源是用于加热的石油,来自电网的电力和用于移动性的柴油。功能单元定义为消耗1公斤氢气。常规燃料的成本是从市场价格中获得的。常规燃料的量是基于从1千克氢气中获得的相同能量来计算的。所考虑的系统边界包括氢气生产过程,氢气运输和氢气消耗。在每个阶段,数据都是从项目合作伙伴和设备供应商/制造商那里收集的。氢气的成本是通过氢气生产和消耗的生命周期来计算的。为了提供具有成本竞争力的解决方案,估计了氢气的建议价格。如果目的是供热(通过锅炉),则在不考虑CO2排放成本的情况下,竞争性氢价估计在1.22英镑/千克至1.28英镑/千克之间。如果目的是通过燃料电池单元提供电能和热量,那么有竞争力的氢气价格在1.48英镑/千克和2.97英镑/千克之间,而无需考虑二氧化碳排放成本。如果将氢气用作氢燃料电池汽车的燃料,则不考虑或考虑二氧化碳排放成本的情况下,氢气的竞争价格水平估计为8.85英镑/千克和8.46英镑/千克。氢技术和常规技术之间的动力或流动性服务,得出的结论是,流动性是氢最接近传统技术的成本有吸引力的命题的应用,即使用柴油作为能源的流动性。在目前的情况下,无论是出于供热目的还是出于电力目的,氢都没有接近成本竞争力。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号