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Database statistics

last update : 51 minutes ago

4

standards

24,080

projects

11,649

participants

28

technologies

1,271,129,728

issued credits

Tianji Group Line 3 N2O Abatement Project

Technology

N2O

Industrial Processes

Industrial Processes | N2O

Country

China

Asia

China

Standard

CDM

Compliance

Stage

Issuance

2012-11-08

CERs issued

Total issued

1,815,580

tCO2

Annual Reduction

523,900

tCO2/year

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CDM

Scope

Chemical industries

Additionality

Tool version :3
Barrier analysis:no
Investment analysis :-Simple Cost Analysis

Provider ID

UNEPcdm1790
UNFCCC1441
Methodology Ver Description
AM00342Catalytic reduction of N2O inside the ammonia burner of nitric acid plants
AM00342Catalytic reduction of N2O inside the ammonia burner of nitric acid plants

Description

The proposed project, Tianji Group Line 3 N2O Abatement Project (hereafter, the Project), is being developed by EcoSecurities Group Plc, Vitol S.A. and Tianji Coal Chemical Industry Group 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 • The awareness of local residents regarding environmental protection will be enhanced through a series of training sessions for plant staff whose family members are local residents;

• The applied monitoring system for N2O emissions will follow the European Standard EN 14181, 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 technical and organisational capacity of domestic contractors.

Plant information

The existing production unit at the Project Developer’s nitric acid plant was a brand new unit when it was first installed in this plant. The burner was manufactured by HarBin Boiler Co. Ltd. It is a type of Medium, dual pressure unit, which began operation on 18th February 2003. Some key information about this plant is shown in Table 1.

Table 1. Key parameters of the production unit at the nitric acid plant

Design capacity                                    902 tHNO3/day (100%), 330 days per year Reactor pressure                                   Dual pressure, medium
Number of burners                                  2
Production in campaign 1(tHNO3 100%)               126,801 (05/06/2004-11/12/2004)
Production in campaign 2(tHNO3 100%)               (81,641)* (13/12/2004-06/04/2005)
Production in campaign 3(tHNO3 100%)               131,566 (26/06/2005-25/12/2005)
Production in campaign 4(tHNO3 100%)               94,407 (08/01/2006-10/05/2006)
Production in campaign 5(tHNO3 100%)               167,742 (12/06/2006-26/01/2007)
Average production in previous 4 campaigns         130,129 (tHNO3 100%) (*Data in campaign 2 is excluded due to its abnormality, data to be audited by verifying DOE, and subject to change accordingly. )
Average production days in previous 4              155 campaigns (days)

(To be audited by verifying DOE, and subject to change accordingly. )

The training of the plant staff has been undertaken in order to ensure the proposed project is in compliance with the methodology AM0034 VER02. 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

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  • 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 283 days
In registration 76 days
To be registered 359 days
To first issuance 591 days
Total to first issuance 948 days

Location

5 Organizations (6 roles involvement)

Certification Participant name CertificationVerifier ()NorwayContact name
Carbon+%26+Environment Participant name Carbon & EnvironmentCredit Buyer ()United KingdomContact name
Carbon+%26+Environment Participant name Carbon & EnvironmentPDD Consultant ()United KingdomContact name
Certification Participant name CertificationValidator ()United KingdomContact name
Finance Participant name FinanceCredit Buyer ()SwitzerlandContact name
Industry Participant name IndustryProject Owner ()ChinaContact name

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