eb58_repan22_ams-iii[一].h_ver16

上传人:小** 文档编号:47691675 上传时间:2018-07-04 格式:PDF 页数:32 大小:351.09KB
返回 下载 相关 举报
eb58_repan22_ams-iii[一].h_ver16_第1页
第1页 / 共32页
eb58_repan22_ams-iii[一].h_ver16_第2页
第2页 / 共32页
eb58_repan22_ams-iii[一].h_ver16_第3页
第3页 / 共32页
eb58_repan22_ams-iii[一].h_ver16_第4页
第4页 / 共32页
eb58_repan22_ams-iii[一].h_ver16_第5页
第5页 / 共32页
点击查看更多>>
资源描述

《eb58_repan22_ams-iii[一].h_ver16》由会员分享,可在线阅读,更多相关《eb58_repan22_ams-iii[一].h_ver16(32页珍藏版)》请在金锄头文库上搜索。

1、UNFCCC/CCNUCC CDM Executive Board III.H./Version 16 Sectoral Scope: 13 EB 58 Indicative simplified baseline and monitoring methodologies for selected small-scale CDM project activity categories 1/32 TYPE III - OTHER PROJECT ACTIVITIES Project participants shall apply the general guidelines to SSC CD

2、M methodologies and information on additionality (attachment A to Appendix B) provided at mutatis mutandis. III.H. Methane recovery in wastewater treatment Technology/measure 1. This methodology comprises measures that recover biogas from biogenic organic matter in wastewater by means of one, or a c

3、ombination, of the following options: (a) Substitution of aerobic wastewater or sludge treatment systems with anaerobic systems with biogas recovery and combustion; (b) Introduction of anaerobic sludge treatment system with biogas recovery and combustion to a wastewater treatment plant without sludg

4、e treatment; (c) Introduction of biogas recovery and combustion to a sludge treatment system; (d) Introduction of biogas recovery and combustion to an anaerobic wastewater treatment system such as anaerobic reactor, lagoon, septic tank or an on site industrial plant;1 (e) Introduction of anaerobic w

5、astewater treatment with biogas recovery and combustion, with or without anaerobic sludge treatment, to an untreated wastewater stream; (f) Introduction of a sequential stage of wastewater treatment with biogas recovery and combustion, with or without sludge treatment, to an anaerobic wastewater tre

6、atment system without biogas recovery (e.g. introduction of treatment in an anaerobic reactor with biogas recovery as a sequential treatment step for the wastewater that is presently being treated in an anaerobic lagoon without methane recovery). 2. In cases where baseline system is anaerobic lagoon

7、 the methodology is applicable if: (a) The lagoons are ponds with a depth greater than two meters, without aeration. The value for depth is obtained from engineering design documents, or through direct measurement, or by dividing the surface area by the total volume. If the lagoon filling level vari

8、es seasonally, the average of the highest and lowest levels may be taken; (b) Ambient temperature above 15C, at least during part of the year, on a monthly average basis; 1 Other technologies in Table 6.3 of Chapter 6: Wastewater Treatment and Discharge of 2006 IPCC Guidelines for National Greenhous

9、e Gas Inventories are included. UNFCCC/CCNUCC CDM Executive Board III.H./Version 16 Sectoral Scope: 13 EB 58 Indicative simplified baseline and monitoring methodologies for selected small-scale CDM project activity categories III.H. Methane recovery in wastewater treatment (cont) 2/32 (c) The minimu

10、m interval between two consecutive sludge removal events shall be 30 days. 3. The recovered biogas from the above measures may also be utilised for the following applications instead of combustion/flaring: (a) Thermal or mechanical,2 electrical energy generation directly; (b) Thermal or mechanical,

11、electrical energy generation after bottling of upgraded biogas, in this case additional guidance provided in Annex 1 shall be followed; or (c) Thermal or mechanical, electrical energy generation after upgrading and distribution, in this case additional guidance provided in Annex 1 shall be followed:

12、 (i) Upgrading and injection of biogas into a natural gas distribution grid with no significant transmission constraints; (ii) Upgrading and transportation of biogas via a dedicated piped network to a group of end users; or (iii) Upgrading and transportation of biogas (e.g. by trucks) to distributio

13、n points for end users. (d) Hydrogen production; (e) Use as fuel in transportation applications after upgrading. 4. If the recovered biogas is used for project activities covered under paragraph 3 (a), that component of the project activity can use a corresponding methodology under Type I. 5. For pr

14、oject activities covered under paragraph 3 (b), if bottles with upgraded biogas are sold outside the project boundary, the end-use of the biogas shall be ensured via a contract between the bottled biogas vendor and the end-user. No emission reductions may be claimed from the displacement of fuels fr

15、om the end use of bottled biogas in such situations. If however the end use of the bottled biogas is included in the project boundary and is monitored during the crediting period CO2 emissions avoided by the displacement of fossil fuel can be claimed under the corresponding Type I methodology, e.g.

16、AMS-I.C “Thermal energy production with or without electricity”. 6. For project activities covered under paragraph 3 (c) (i), emission reductions from the displacement of the use of natural gas are eligible under this methodology, provided the geographical extent of the natural gas distribution grid is within the host country boundaries. 2 For example combusted in a prime mover such as an engine coupled to a machine such as gr

展开阅读全文
相关资源
相关搜索

当前位置:首页 > 商业/管理/HR > 经营企划

电脑版 |金锄头文库版权所有
经营许可证:蜀ICP备13022795号 | 川公网安备 51140202000112号