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Learn moreShijiazhuang Jinshi N2O Abatement Project
Technology
N2O
Industrial Processes

Country
China
Asia

Standard
CDM
Compliance
Stage
Issuance
2011-03-23
CERs issued
Total issued
303,114
tCO2
Annual Reduction
198,545
tCO2/year
CDM
Scope
| Chemical industries |
Additionality
| Tool version : | 3 |
| Barrier analysis: | no |
| Investment analysis : | -Simple Cost Analysis |
Provider ID
| UNEP | cdm1824 |
| UNFCCC | 1612 |
| Methodology | Ver | Description |
| AM0034 | 2 | Catalytic reduction of N2O inside the ammonia burner of nitric acid plants |
| AM0034 | 2 | Catalytic reduction of N2O inside the ammonia burner of nitric acid plants |
Description
The proposed project, Shijiazhuang Jinshi N2O Abatement Project (hereafter, the Project), is developed by EcoSecurities Group Plc and the Shijiazhuang Jinshi Chemical Fertilizer Co. Ltd (hereafter referred to as the Project Developer). The purpose of the Project is to reduce the current levels of N2O emissions at the Project Developer’s fertilizer plant during the production of nitric acid (HNO3).
Nitrous Oxide (N2O) is an undesired by-product emitted from the production of nitric acid (HNO3), which is formed during the catalytic oxidation of ammonia. N2O is directly released into the atmosphere from nitric acid production plants without any treatment, as it does not have any economic value or toxicity. N2O is however recognised as a potent greenhouse gas with a Global Warming Potential (GWP) of 310 compared to carbon dioxide (CO2), and currently is responsible for approximately 6% of the greenhouse effect1. The production process of nitric acid typically generates N2O quantities of 2-19 kg per tonne of pure anhydrous nitric acid (100%)2, thus not removing N2O from the production of nitric acid has a large potential for global warming.
The Project will use the secondary N2O abatement catalyst technology which involves the installation of a secondary catalyst in the burner basket. The secondary catalyst will be located beneath the ammonia oxidation catalyst gauzes, and through this secondary catalyst N2O will be converted into Nitrogen (N2) and Oxygen (O2) which have no adverse environmental or human health impacts.
The Project will produce environmental and economic benefits, which will contribute to the sustainable development of the Host Country. The specific sustainable development benefits of the Project are as follows:
• A new technology will be transferred to the Host Country, reflected in the installation of an N2O abatement technology, which will include a novel N2O abatement catalyst and monitoring system/equipment. Furthermore, the local plant staff will be trained to operate this new equipment; • The awareness of local residents regarding environmental protection will enhance through a series of training sessions to plant staff whose family members are the local residents; • The applied monitoring system for N2O emissions will follow the European Standard EN14181, which is not only new for the Project Developer and for the Host Country, but also novel in Europe. By following the quality assurance of the automated measuring systems, the local employees will build capacity in these quality management techniques that are not yet widely spread in the Host Country;
• The commissioning and operation of monitoring equipments and catalyst will contribute to the creation of the technical and organisational capacity of domestic contractors.
Plant information
The nitric acid production unit was brand new when it was first installed at the current site. It started the operation on the 6th September 2005. It is a medium, dual pressure unit with design capacity of 350 tonnes of HNO3 (100%) per day. The operating time is 330 days a year. Some information about this plant is shown in Table 1.
Table 1. Information of the nitric acid plant Design capacity 350 tHNO3/day (100%), 330 days per year Reactor pressure Dual pressure, medium
Number of burners 1
Production in campaign 1(tHNO3 100%) 46,380 (06/09/2005-09/03/2006)
Production in campaign 2(tHNO3 100%) 56,990 (14/03/2006-17/10/2006)
Production in campaign 3(tHNO3 100%) 68,440 (27/10/2006- 03/05 /2007)
Average production in previous 3 campaigns 57,270 (tHNO3 100%) (Data to be audited by verifying DOE, and subject to change accordingly )
Normal production days for one set of primary 180days gauze
The training of the plant staff has been undertaken in order to ensure the proposed project is compliance with the methodology AM0034 VER 02. Details regarding the content and future plans of the training are described in the Monitoring Manual, which will be available for the verifying DOE during the verification. A summary of the training plan can be found in the monitoring plan in Annex 4.
Technicals
Investment
$0
Energy
| Installed capacity | 0 MW |
| Effective hours | - |
| Energy generated | 0 MWh/year |
| Utilization ratio | 0 % |
| Activity start date | - |
Time
In validation
: Total elapsed days between “opening comments” and the registration request date.In registration
: Total elapsed days from registration request until approval.To be registered
: Total elapsed days from Validation until Registration approval (Validation + Registration).To first issuance
: Total elapsed days from registration approval until first credit issuance.Total to first issuance
: Sum of entire validation, registration and ‘to first issuance’ days; i.e. the entire process.
| In validation | 329 days |
| In registration | 137 days |
| To be registered | 466 days |
| To first issuance | 995 days |
| Total to first issuance | 1459 days |
Location
4 Organizations (5 roles involvement)
![]() | Participant name | Certification | Verifier | () | Norway | Contact name |
![]() | Participant name | Carbon & Environment | Credit Buyer | () | United Kingdom | Contact name |
![]() | Participant name | Carbon & Environment | PDD Consultant | () | United Kingdom | Contact name |
![]() | Participant name | Certification | Validator | () | Germany | Contact name |
![]() | Participant name | Industry | Project Owner | () | China | Contact name |
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