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Database statistics

last update : 31 minutes ago

4

standards

24,080

projects

11,649

participants

28

technologies

1,271,129,728

issued credits

Catalytic N2O Abatement Project in the tail gas of the Caprolactam production plant in Thailand

Technology

N2O

Industrial Processes

Industrial Processes | N2O

Country

Thailand

Asia

Thailand

Standard

CDM

Compliance

Stage

Issuance

2013-03-09

Request For Issuance

Total issued

281,982

tCO2

Annual Reduction

142,402

tCO2/year

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CDM

Scope

Chemical industries

Additionality

Tool version :5
Barrier analysis:no
Investment analysis :-Simple Cost Analysis

Provider ID

UNEPcdm2179
UNFCCC2232
Methodology Ver Description
AM00284Catalytic N2O destruction in the tail gas of nitric acid or caprolactam production plants
AM00284Catalytic N2O destruction in the tail gas of nitric acid or caprolactam production plants

Description

Caprolactam (C6H11NO) is an important raw material in the production of Nylon 6 which is used in various industries, given its special characteristics. It is very durable and can withstand high temperature well, yet still maintains excellent flexibility. It is used in many different high quality products such as in the textile industry for clothed and swimwear, canvas production, casting nets for deep-sea fishing, etc.

Thai Caprolactam Public Co., Ltd. (hereinafter “TCL”) is the first producer and distributor of caprolactam and ammonium sulphate in Thailand and Southeast Asian region and have operated since the actual caprolactam production had commenced in 1997. And TCL had conducted three production capacity expansions by December 2005. (the design capacity in December 2005: 111,860 tCaprolactam/yr (329[tCaprolactam /day]* 340 [day/yr]) same as the current situation) In TCL, nitrous oxide (N2O) is generated by side reaction of ammonia oxidation reaction of Hydroxylamine production unit, which is intermediate of caprolactam production. Ammonia oxidation section generates NO/NO2 gases by oxidize ammonia with oxygen at Ammonia Oxidation Reactor by precious catalyst gauze.

The aim of the project activity is to reduce N2O emission of the tail gas emitted from Ammonium Nitrite Preparation process 1 by installation of a DeN2O catalyst in TCL. Then, in TCL, NH3 Selective Catalytic Reduction (NH3-SCR) technology has been used to reduce NOx concentration in the tail gas emitted from Ammonium Nitrite Preparation process. SCR reduce around 95% of NOx emissions.

This technology is continued to be used, because of effluent gas compliance with local environmental regulations.

On the other hand, N2O is not a toxic substance and is not regulated in Thailand. Therefore, it has been released to atmosphere without any recovery or any specific treatment at the targeted facility of the TCL. TCL has no plan to implement N2O abatement under such situation if the proposed project would not be implemented as CDM. There is no economic incentive to recover and utilize or sell N2O as a product, technically and economically, except for CERs.

In addition, the project does not result that the amount of production would exceed the design capacity although the production has been and expected to be increased gradually. Therefore, without CERs, TCL will continue releasing N2O to the atmosphere under its normal operation (i.e., will continue the current practice) The project is to introduce catalytic DeN2O equipment at the tail point before release to the atmosphere. The technologies are provided by N.E. Chemcat (catalyst) and SUMITOMO METAL MINING ENGINEERING (engineering). It is expected that the equipment can decompose more than 85% of the N2O, which would be emitted otherwise. 2 In addition to reduce N2O emissions, the project transfers a clean technology which is not yet widely commercialized even in industrialized countries. It also includes the training course for operation of the DeN2O equipment and also for accurate monitoring. The local employment will be created through the direct/indirect economical effects through the project activity.

As for the contribution of sustainable development for local, host country, the N2O abatementechnology will be introduced to the project, which will be beneficial to further promote the application of the advanced technology, which is not yet widely commercialized even in the industrialized countries. Furthermore the implementation of the project activity includes the training course for accurate monitoring, which will provide the staffs of TCL with an opportunity to learnew technology and improve their skills.

Project participants:

Technicals

Investment

$3M

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 466 days
In registration 275 days
To be registered 741 days
To first issuance 834 days
Total to first issuance 1573 days

Location

6 Organizations (7 roles involvement)

Carbon+%26+Environment Participant name Carbon & EnvironmentPDD Consultant ()JapanContact name
Certification Participant name CertificationValidator ()NorwayContact name
Certification Participant name CertificationVerifier ()GermanyContact name
Finance Participant name FinanceCredit Buyer ()RussiaContact name
Industry Participant name IndustryProject Owner ()SpainContact name
Other Participant name OtherCredit Buyer ()JapanContact name
Other Participant name OtherPDD Consultant ()JapanContact name

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