## MONTREAL PROTOCOL

ON SUBSTANCES THAT DEPLETE

THE OZONE LAYER



# UNEP

Chemicals Technical Options Committee

(CTOC)
2010 Assessment Report2010 CTOC Progress Report iii 

### UNEP
R EPORT OF THE 

### C HEMICALS 

### T ECHNICAL 

### O PTIONS 

### C OMMITTEE



### 2010 A SSESSMENT 

### R EPORT2010 CTOC Progress Report iv Montreal Protocol On Substances that Deplete the Ozone Layer



### Report of the UNEP Chemicals Technical Options Committee

2010 Assessment

A SSESSMENT R EPORT

The text of this report is composed in Times New Roman.

Co-ordination: Chemicals Technical Options Committee

Reproduction: Ozone Secretariat, UNEP Date: March 2011

Under certain conditions, printed copies of this report are available from:

UNITED NATIONS ENVIRONMENT PROGRAMME Ozone Secretariat, P.O. Box 30552, Nairobi, Kenya

This document is also available in portable document format from the UNEP Ozone Secretariat's website:

http://ozone.unep.org/Assessment_Panels/TEAP/Reports/CTOC/

No copyright involved. This publication may be freely copied, abstracted and cited, with acknowledgement of the source of the material.

ISBN: 9966-7319-8-92010 CTOC Progress Report v 

### Disclaimer

The United Nations Environmental Programme (UNEP), the Technology and Economic Assessment Panel (TEAP) co-chairs and members, the Technical and Economics Options Committee, chairs, co-chairs and members, the TEAP Task Force co-chairs and members, and the companies and organisations that employ them do not endorse the performance, worker safety, or environmental acceptability of any of the technical options discussed. Every industr ial operation requires consideration of worker safety and proper disposal of cont aminants and waste products. Moreover, as work continues - including additional toxicity evaluation - more information on health, environmental and safety effects of alternatives and replacements will become available for use in selecting among the options discussed in this document.

UNEP, the TEAP co-chairs and members, the Technical and Economic Options Committee, chairs, co-chairs and members, and the Technology and Economic Assessment Panel Task Forces co-chairs and members, in furnishing or distributing the information that follows, do not make any warranty or representation, either express or implied, with respect to the accuracy, completeness or utility; nor do they assume any liability of any kind whatsoever resulting from the use or reliance upon any information, material, or procedure contained herein.

Mention of any company, association, or product in this document is for information purposes only and does not constitute a recommendation of any such company, association, or product, either expressed or implied by UNEP, the Technology and Economic Assessment Panel (TEAP) co-chairs and members, the Technical and Economics Options Committee, chairs, co-chairs and members, the TEAP Task Force co-chairs and members, and the companies and organisations that employ them.2010 CTOC Progress Report vii 

### UNEP
R EPORT OF THE 

### C HEMICALS 

### T ECHNICAL 

### O PTIONS 

### C OMMITTEE



### 2010 A SSESSMENT 

### R EPORT

TABLE OF CONTENTS....................................................................................PAGE

Executive Summary.......................................................................................................1 1, Process Agents ............................................................................................................5
1.1 Revision of Table A and Table B .............................................................................5 1.2 Cooperation between TEAP/CTOC and MLF .....................................................5 2. Laboratory and Analytical Uses ...............................................................................9
2.1 Introduction ..............................................................................................................9 2.2 Status on Laboratory Uses ......................................................................................9 2.3 Status on Analytical Uses .........................................................................................9 2.4 Importance of Standard Analysis .........................................................................10
3. Feedstocks................................................................................................................. 1 1
4. Solvents .................................................................................................................... .13
4.1 Introduction ............................................................................................................13
4.2 Status in Article 5 Countries .................................................................................13 4.3 Regulatory Changes ...............................................................................................14 4.3.1 European Regulation Changes......................................................................14 4.3.2 Japanese Regulation Changes.......................................................................15 4.4 n-Propyl bromide ...................................................................................................15 5. Destruction Technologies.........................................................................................17
5.1 Introduction ............................................................................................................17 5.2 Recent Progress ......................................................................................................17 5.2.1 Environmentally Sound Management of Banks of ODS .............................17 5.2.2 Update of the screened-in destruct ion technologies of 2002 TF Report ......18
5.2.3 Article 5 countries.........................................................................................18 5.2.4 Evaluation of reported emerging technologies .............................................19 6. Carbon Tetrachloride (CTC) Emissions and Opportunities for Reduction.......202010 CTOC Progress Report 1 

### Executive Summary

Process Agents

In the last four years more than seventy process agent applications have been reviewed by the CTOC (see annex 1) . Parties have approved 17 process agent uses which are added to Table A. Also, 12 uses have been deleted from Table A as processes were abandoned or modified, often (but not always) as a result of MLF projects (Decisions XIX/15 and XXI/3)

.

As late as 2009, nominations for process agent status were still being received as
Parties became aware of activities of th eir chemical industry sectors in which
controlled substances were used. Reporting of emissions to Table B has been less than complete.

A better standard of reporting of emissions needs to be achieved so that Table B gives a more reliable picture of emissions arising from process agent uses. When the CTOC and MLF will produce a joint report in 20 11 according to the Decision XXI/3 (5),
further deletions from Table A and a more complete update on phase-outs or suggestions for phase-outs could be possible.

A list of Parties with approved process agent uses could be provided to the Ozone Secretariat, so that requests for informatio n could be targeted and followed up, rather than including such requests in global communications.

Laboratory and Analytical Uses

There are very few identified uses of ODS in laboratory and analytical procedures in
non-Article 5 countries. Some use continues in several Article 5 countries.

Advice by experts is required, together with modest financial support for alternatives that have already been identified to be triall ed in Article 5 countries, alongside current procedures that involve ODS. New standard methods need to be developed.

Advice delivered by experts to practitioners at laboratory level is most valuable. It can be augmented by national or regional meetings, by provision of advice through electronic means, and via information transf er involving ozone officers. It would be helpful to the phaseout for th e Ozone Secretariat and experts identified by the CTOC to
work with national and international stan dards bodies to establish new standard methods of analysis that do not use ODS. TEAP and the CTOC will keep Parties
informed of advances on these fronts.2010 CTOC Progress Report 2 Feedstocks

An extensive listing of known use of ODSs as feedstocks has been compiled. Using volumes suggested by members of the CTOC and following guidelines for emission calculations suggested by the IPCC for the UNFCCC, estimates of emissions from these feedstocks have been generated.

The volumes used in the report have been built up from expert knowledge and cannot be verified directly. There is poor reporting of use of ODSs as feedstocks. Also, at the current time, the majority of the productio n from ODS feedstocks is for HFCs whose production is not reported to a public source of data. To improve the estimate of use and emissions, it will be necessary to iden tify more complete public sources or for all Parties to report feedstock usage. In addition, the IPCC guidelines to not well represent actual emissions during use of ODS as feedstock. Expert opinion suggests that the IPCC guidelines are maximal values and actual emissions may be lower at well managed facilities. Better emission mechanisms need to be considered.

Developed countries report to UNFCCC emission data for HFCs in their inventory reporting. Thus, discussions with UNFCCC may assist in developing new estimated sources of data for HFC production (which may have utilized ODSs as feedstock in their preparation). The reporting of ODS vo lumes for each feedstock uses by Parties through the Ozone Secretaria t may enable a more complete quantification of this activity.

Solvents

Over 90 % of ODS solvent uses based on the peak consumption of 1994-95 have been reduced by changing to not- in-kind technologies and conservation. The remaining less than 10% of the ODS market is shared by several in-kind solvent alternatives.

The major challenge is the complete phase out of ODS solvents in Article 5 countries.
Preferable alternatives have been identified and are generally available. Another hurdle to overcome is the economic impact on the small and medium size users who make up a major portion of the remaining ODS solvent market.

Regulatory changes will continue to impact on the use of solvents. In some cases, this may require solvent and/or equipment change or a new cleaning process. New idea of the definition of low-GWP and high-GWP alternatives which TEAP proposed may cause a profound effect on the use of solvent.

Destruction Technologies

In 2009, CTOC identified 176 destruction facilities in 27 countries including new technologies not listed in the 2002 Task Force Report.

Recently several emerging technologies have been requested for evaluation. Following Decision XXI/10, they will be reviewed when technical details are made available.2010 CTOC Progress Report 3 Periodic review of available destruction technologies will be necessary to provide updated technical guidelines for destruction of ozone depleting substances such as CFCs, halons and methyl bromide as well as for HFCs.

Carbon Tetrachloride (CTC) Emissi ons and Opportunities for Reduction

The TEAP/CTOC made a comprehensive review on CTC emissions, concluding that there is a significant discrepancy betwee n reported emissions and the observed atmospheric concentrations under Decisions XVI/14 and XVIII/10.

The studies have not yet been completed on the production and consumption of CTC with particular emphasis on feedstock uses with the goal to estimate emissions and try to reconcile them with values calculated by atmospheric scientists.

No new information on CTC emission was obtained in the course of the CTOC activities by 2010. Further studies will be needed to improve and reconcile bottom-up and top-down calculations, to search for other unreported CTC emission sources, to revise the UNEP inventory data and to furt her revise the atmospheric lifetime of CTC.2010 CTOC Progress Report 5 

### 1. Process Agents

1.1 Revision of Table A and Table B

Nominations for process agent uses have been reviewed by two Process Agent Task Forces (2001 and 2004) and since then by the CTOC as part of TEAP’s annual progress reports. In the last four years, more than seventy process agent applications have been reviewed by the CTOC (see Annex 1) . The Parties approved and added 17 process agent uses to Table A in Decision X/14. At the same time, 12 uses were deleted from the Table A as the processes were abandoned or modified, often (but not always) as a result of MLF projects (Decisions XIX/15 and XXI/3) . As late as 2009, nominations for process agent status were received as Partie s became aware of old or new activities of their chemical industry sectors in wh ich controlled substances were used.

Information of ODS emissions from process agent uses in Table B has been less than complete. A better standard of reporting of em issions needs to be achieved so that table B gives a reliable picture of emissions arising from process agent uses.

1.2 Cooperation between TEAP/CTOC and MLF

Based on the further information from reports of the MLF projects, the following seven process agent applications, No. 4, 9, 17, 21, 23, 25 and 26 in the
column of Decision XXI/3 in Annex 1, could be removed because Parties no longer operate facilities requiring these processes.. When the CTOC and MLF produce a joint report in 2011 (Decision XXI/3), a more complete update on phase-out or suggestions for phase-out will be achieved.

A list of Parties with approved process agen t uses could be provided to the Ozone Secretariat, so that requests for nece ssary information could be targeted.

Parties and the MLF should prioritise effort s on eliminating those process agent uses that have the highest emissions.2010 CTOC Progress Report 6 Annex 1: Table of the reviewed list of uses of controlled substances as process agents (status through 2010 decisions)

Process Agent

Application Substance Decision

XVII/7 Decision

XVII/8 Decision

XIX/15 Decision

XXI/3 Decision

XXII/-***

Elimination of NCl 3 in chlor-alkali production CTC 1 1 1 1

Chlorine gas recovery by tail gas absorption in chlor-alkali production CTC 2 2 2 2

Production of chlorinated rubber CTC 3 3 3 3

Production of Endosulfan CTC 4 4 4 4 Production of Ibuprofen CTC 5 5 5 **
Production of Dicofol CTC 6 6 **
Production of ch lorosulfonated polyolefin (CSM) CTC 7 7 6 5

Production Aramid polymer (PPTA) CTC 8 8 7 6 Production of fluoropolymer resins CFC-113 9 ** Production of synthetic fibre sheet CFC-11 10 9 8 7

Production of styrene butadiene
rubber CTC 11 **

Production of chlorinated paraffin CTC 12 10 9 8 Photochemical synthesis of perfluoropolyetherpolyperoxide precursors of Z-perfluoropolyethers
and difunctional derivatives CFC-12 13 11 10 9

Reduction of perfluoropolyetherpolyperoxide

intermediate for production of

perfluoropolyether diesters CFC-113 14 12 11 **

Preparation of perfluoropolyether diols with high functionality CFC-113 15 13 12 10

Production of Bromohexine hydrochloride CTC 16 **

Production of Diclofenac sodium CTC 17 **

Production of phenyl glycine CTC 18 **

Production of Cyclodime CTC 19 14 13 11
Production of chlorinated polypropene CTC 20 15 14 12

Production of chlorinated ethylene vinyl acetate (CEVA) CTC 21 16 15 13

Production of methyl isocyanate
derivatives CTC 22 17 16 14

Production of 3-phenoxy benzaldehyde CTC 23 18 17 15

Production of 2-chloro-5-methylpyridine CTC 24 19 18 162010 CTOC Progress Report 7 Process Agent

Application Substance Decision

XVII/7 Decision

XVII/8 Decision

XIX/15 Decision

XXI/3 Decision

XXII/-*** Production of Imidacloprid CTC 25 20 19 17 Production of Buprofenzin CTC 26 21 20 18
Production of Oxadiazon CTC 27 22 21 19
Production of chloradized N-methylaniline CTC 28 23 22 20

Production of Mefenacet CTC 29 ** Production of 1,3-
dichlorobenzothiazole CTC 30 24 23 21

Bromination of a styrenic polymer BCM 31 25 24 22 Synthesis of ascorbic acid CTC 32 ** Synthesis of Ciprofloxacin CTC 33 **

Synthesis of Norfloxacin CTC 34 ** Synthesis of 2,4-dichlorophenoxyacetic acid (2,4-D) CTC 35 26 25 23

Synthesis of diperoxydicarbonate CTC 36 **
Production of sodium dichloroisocyanurate CTC 37 **

Synthesis of di(-2-ethylhexyl)peroxidedicarbonate (DEHPC) CTC 27 26 24

Production of radio-labelled cyanocobalamin CTC 38 28 27 **

Production of high modulus polyethylene fibre CFC-113 39 29 28 25

Production of vinyl chloride

monomer CTC 30 29 26

Production of p-bromobenzaldehyde CTC 40 *
Production of fenvalerate CTC 41 *
Manufacture of Losartan Potassium BCM 42 *
Production of 1,2-chloro-1,4-naphthoquinone CTC 43 *

Production of Prallethrin CTC 44 32 31 28
Production of 2-methoxybenzoylchloride CTC 45 *

Production of o-nitrobenzaldehyde CTC 46 33 32 29
Production of Salimusk CTC 47 * Production of Epoxiconazole CTC 48 * Production of benzophenone CTC 49 * Production of Picloram; Lontrel CTC 50 *
Production of 3-methyl-2-thiophenecarboxaldehyde CTC 51 34 33 30

Production of Difenoconazole CTC 52 *2010 CTOC Progress Report 8 Process Agent Application Substance Decision

XVII/7 Decision

XVII/8 Decision

XIX/15 Decision

XXI/3 Decision

XXII/-***
Production of 2-thiophenecarboxaldehyde CTC 53 35 34 31

Production of 2-thiophene ethanol CTC 54 36 35 32
Production of 5-amino-1,2,3-thiadiazol CTC 55 *

Production of Levofloxacin CTC 56 *
Production of cinnamic acid CTC 57 *
Production of Ertaczo CTC 58 * Production of 3,5-dinitrobenzoyl chloride (3,5-DNBC) CTC 59 37 36 33

Production of Fipronil (pesticide) CTC 60 * Processing of Aluminium, Uranium CTC, CFC 61 *
Production of furfural CTC 62 * Production of 3,3,3-trifluoropropene CTC 63 *
Production of triphenylmethylchloride CTC 64 *

Production of tetrachlorodimethylmethane CTC 65 *

Production of 4,4`-difluorodiphenylketone CTC 66 *

Production of 4-trifluoromethoxybenzenamine CTC 67 *

Production of 1,2-benzisothiazol-3-ketone CTC 68 38 37 34

Production of Sultamicillin BCM 31 30 27
Production of m -nitrobenzaldehyde CTC 39 38 35 Production of Tichlopidine CTC 40 39 36
Production of p -nitro benzyl alcohol CTC 41 40 37 Production of Tolclofos methyl CTC 42 41 38

Production of polyvinylidene fluoride (PVdF) CTC 42 39

Production of tetrafluorobenzoylethyl acetate CTC 43 40

Production of 4-bromophenol CTC 44 41

* Do not meet criteria X/14,
** Phased out *** Three applications was deleted from Table A (Decision XXI/3, #5, 11 and 27) in the 22 nd MOP in Bangkok, Thailand

.2010 CTOC Progress Report 9 

### 2. Laboratory and Analytical Uses

2.1 Introduction

Parties continued to show interest in the use of ODS for laboratory and analytical purposes. In 2007, Decision XIX/8 extended the global exemption to 31 December 2011, and then in 2009 the global exemption for all Parties was extended to 31 December 2014, with the exception of a fe w procedures for which it was agreed that
suitable alternatives were available.

On several occasions the CTOC was asked to describe the uses and to provide lists of suitable alternatives, and much information of this type was made available in the annual TEAP reports. The 2009 TEAP Progress Report contained information about case studies in Australia, European Union, Japan and the United States, showing the way that Parties managed such uses and, in some cases, had eliminated them.

2.2 Status on Laboratory Uses

There are laboratory uses of some ODS – notably methyl bromide (MB) and carbon tetrachloride (CTC) – for which it is difficu lt to find alternatives because portions of the ODS molecules are incorporated in the products of the chemical reactions. Since the ODS are destroyed, through conversio n to non-ODS products, and laboratory procedures are in any case conducted on a mu ch smaller scale than those in industry, the likely emissions from such uses are small.

Despite some trials by interested laboratories, there is one laboratory solvent use of CTC for which does not yet have an altern ative (bromination reactions using N-bromosuccinimide).

Other laboratory uses of ODS, as common so lvent or cleaning agent, for example, have largely been phased out in developed countries and are disappearing from laboratories in developing countries, by alternatives with similar polarity and solvent properties

2.3 Status on Analytical Uses

The most common analytical procedures usin g ODS is use of CTC (and in some cases CFC-113) as a solvent for infrared analys es of hydrocarbons. The hydrocarbons in question are those involved in contamination of water, soil or air by petroleum-derived
oils. The best alternative to CTC is tetr achloroethylene (perchloroethylene) which has been shown to perform satisfactorily in such analyses and is widely available in global markets. This alternative was suggested by the CTOC and the trials were successfully conducted in an Article 5 country. A new commercial product (S-316) that can also substitute for CTC is also available on world markets, but it is expensive and many users of CTC, especially in Article 5 countr ies, have not switched to the new analytical
medium. Alternatives have also been id entified for other analyses using CTC or 1,1,1-trichloroethane (TCA), and introduced into practice in a number of countries.2010 CTOC Progress Report 10 CTOC members, supported by implementing agencies as UNDP and UNIDO, have provided advice and guidance to laboratory personnel and ozone officers, directly or advising through regional networks meetings.

2.4 Importance of Standard Analysis

The reluctance of analytical laboratories to replace CTC in hydrocarbon analysis, while there may be a cost factor, arises from th e fact that CTC is sp ecified in standard analytical methods that have great valu e in quality assuran ce and quality control (QA&QC). Assurance that an analysis has been done properly and the result is repeatable and may be compared with other results obtained by standard analysis is an important tenet of analytical chemistry. Such assurance is sought by company management, who are aware that customers who purchase a company’s products, and regulators who monitor environmental performance, will insist that results be reported
on the basis of standard methods.

There is a need, therefore, for the developm ent of new standard methods, ones that do not involve the use of ODS. By the other hand, some standard methods present one or more alternative solvents to ODS, but there is need of awareness activities, in order to
make trials and validate those methods with the alternatives. The Ozone Secretariat, in conjunction with the CTOC, is engaged wi th national and international standards associations in the development of new methods of analysis.2010 CTOC Progress Report 11 

### 3. Feedstocks

An extensive listing of known use of ODSs as feedstocks has been compiled. These are for products as diverse as other fluorochemicals, polymers and films, pharmaceuticals, fine chemicals, etc. The CTOC has estimated emissions from feedstock use based on expert knowledge and utilizing guidelines for emission calculations suggested by the
IPCC for the UNFCCC.

The volumes estimated in the report have been built up from expert knowledge and cannot be verified directly. There is poor reporting of use of ODSs in feedstocks. Also, at the current time, the majority of the f eedstock use is for the production of HFCs which have no publicly reported data on the amount of production. To improve the estimate of use and emissions it will be necessary to identify more complete public sources or for all Parties to report feedstock usage. In addition, it is felt that the IPCC guidelines to not well represent actual em issions during use of ODS as feedstock. Expert opinion suggests that the IPCC guidelines are maximal values and actual emissions from well managed plants are lower. Better emission mechanisms need to be
considered.

Developed country Parties to UNFCCC re port emission data for HFCs in their inventory reporting, discussions with UNFCCC may assist in developing new sources of data for HFC production (which may ha ve utilized ODSs as feedstock in their preparation). The reporting by Parties of ODS volumes used as feedstocks through the Ozone Secretariat may enable a more complete quantification of this activity. Alternatively, inquiries to select Parties mi ght improve understanding of this activity.2010 CTOC Progress Report 13 

## 4. Solvents

4.1 Introduction

As is reported in the IPCC/TEAP SROC, ov er 90% of the ODS so lvent use had been reduced through conservation a nd substitution with not-in-kind technologies by 1999. The phaseout of the remaining less than 10% of the original solvent use are shared by several organic solvent alternatives, especially by the in-kind alternatives to CFC-113 which include HCFCs, HFCs and HFEs (hydro fluoroethers) with minimal use of PFCs such as perfluorohexane in non-Article 5 countries.

Not-in-kind alternatives options include no- clean mainly in electronics and aerospace, aqueous systems in degreasing and precisi on cleaning, hydrocarbon in precision mechanics and oxygenated solvents in diverse cleaning applications. The primary substitutes for 1,1,1-trichloroethane (TCA ) and CTC cover chlorocarbon alternatives such as trichloroethylene, perchloroethylene and methylene chloride. Also, a brominated substance, n-propyl bromide, with similar solvent properties to those of the chlorinated solvents, has taken a significant market share in recent years for defluxing, general cleaning and adhesives applications in spite of its concerned toxicity.

The in-kind substitutes for CFC-113 and CFC-11 are fluorinated alternatives such as hydrochlorofluorocarbons (HCFC-141b and HCFC-225ca/cb), perfluorocarbons (primarily C6F14), hydrofluorocarbons (HFC-43-10mee, HFC-365mfc and HFC-245fa, HFC-c447ef) and hydrofluoroethers (HFE-449 s1, HFE-569sf2). HFCs are available in all regions but their uses have been primarily in non-Article 5 countries due to relatively high cost and importance of high tech industries. Their growth is expected to be minimal due to the increasing concern about their high GWP. In Article 5 countries, use of HCFC-141b has been increasing especi ally in China, India, and Brazil and its consumption exceeded 5,000t.

4.2 Status in Article 5 Countries

As shown in UNEP database, consumption and production amount of ODSs in Annex A and Annex B have been decreasing steadily in Article 5 countries. Although the complete phase out of those substances has not come yet, progress in achieving the phase-out in Article 5 countrie s has been good, given the widespread use of ozone-depleting solvents and the variety an d complexity of their applications. Of the various uses, the large-scale electronics in dustry has progressed furthest towards a complete phase-out, although this is not the case with small- and medium-sized enterprises (SMEs). Full phase-out for metal cleaning applications is hampered by the large number of small users, many of whom are undercapitalised. In precision cleaning applications, users have been aggressively implementing alternatives. Some enterprises are still searching for solutions for cleanin g precision parts that are especially vulnerable to residues or reactions, or that have unusually stringent cleanliness criteria.

The challenges that are facing the world ar e complete phase out of ozone depleting
substances in Article 5 countries. Preferable alternatives have been identified2010 CTOC Progress Report 14 throughout the world and are generally read ily available, so to keep providing information and knowledge about what ar e the acceptable alternatives is quite important. A second major hurdle to be overcome is the economic considerations. However, the biggest problem is being able to identify the SMEs that, collectively, make up a major portion of the solvent market. The remained issue to note is promotion of the replacement process of essential uses in
non Article 5 countries.

The selection of the alternative technologies to ODS solvents for Article 5 countries
should be:

• "No-clean", keep-clean

• Aqueous/hydrocarbon-surfactant cleaning

• Organic solvent cleaning (with solvents less toxic than non-ozone-depleting halogenated solvents)

• Non-ozone-depleting halogenated so lvents (HFC, HFEs, TCE, PCE)

• Organic solvent cleaning (with solvents more toxic than non-ozone-depleting halogenated solvents

• HCFC-225, and some PFCs

All applications to the Multilateral Fund that propose the use of aqueous or hydrocarbon surfactant cleaning require funding for pollution prevention, recycling, waste water treatment, shower and eye-wash facilities and drying equipment, as appropriate. Applications that involve the use of organic and hydrogenated solvents require containment equipment, adequate ventilation control, and/or low emission equipment. The guidelines for all processe s should include requirements for personnel safety, for example, the use of eye guards and other personal protection equipment by workers who perform the cleaning operation and means for the measurement of
operator exposure.

4.3 Regulatory Changes

The regulatory changes continue to impact use of solvents as well as containment, emission, safety, health and recycling requirements. In some cases, they may require solvent and/or equipment change or a new cleaning process. The new definition of low-GWP and high-GWP alternatives which TEAP proposed this year may cause a profound effect on the remaining use of ODS and HFC solvents.

4.3.1 European Regulation Changes

Regulation on F-gases came into effect in 2006 in EU, covering refrigerants in automobiles. The new European chemical policy called REACH (Registration Evaluation and Authorization of Chemicals) came into effect as a new regulation in mid 2007. It could impact substances availa bility for certain uses (including solvents) in cases where low sales volumes cannot support the testing regime required by REACH or where the re-assessed properties of the substance militate against its use. New regulation on CLP (Classification, Labelling and Packaging) will come in this December, where ODSs, such as CFCs, halons, CTC, Methylchloroform, HFBCs and HCFCs, are classified as hazardous to the ozone layer2010 CTOC Progress Report 15 4.3.2 Japanese Regulation Changes

The PRTR (Pollutant Release and Transfer Register) regulation which came into effect in 2002 requires reporting of release and transfer of 354 substances including all ODSs and chlorinated solvents. The other regulation which has a major effect in controlling cleaning operation is the VOC (volatile or ganic compound) regulation. It came into effect from April 2006. The quantity of VOC s emitted in industrial cleaning in 2007 was 124,000 tons. Of those VOCs emitted, 35% was chlorinated solvents such as methylene chloride (17%), trichloroethylene (10%) and perchloroethylene (4%). In order to achieve reduction in emission, va rious combinations of cleaning equipments, operating manuals and peripherals to suit the processes are needed and efforts are made to develop such systems.

4.4 n-Propyl bromide

Concerns have been expressed during th e current assessment period about the increasing use of n-propyl br omide (1-bromopropane, CH 3 CH 2 CH 2 Br, n-PB, CAS No. 106 94 5) as a solvent in a range of applications. Its boiling point, 71 o C, is comparable to that of CFC-113 (48 o C), hexane (69 o ), methyl chloroform (TCA, 74 o C) and trichloroethylene (87 o C). Its solvent properties ar e typical of those of lower molecular weight hydrocarbons and organohalogen compounds.

Because of the presence of bromine in the molecule there is the potential for ozone depletion arising from transfer of n-PB to the stratosphere, and decomposition there with release of bromine atoms. Analogie s are drawn with methyl bromide, a lower homologue of n-PB which finds extensive use as a fumigant and has ozone depleting potential (ODS) of 0.6. The intermediate homologue, ethyl bromide, has few
commercial uses.

Complete and accurate data on production and uses of n-PB have been difficult to obtain. The global production level was estimated to be 20,000-30,000 metric tonnes in 2007, with production taking place in severa l A(5) and non-A(5) co untries. n-PB is not classified or registered as a controll ed chemical substance like CFCs, and HCFCs (ODS class I and II) nor designated as a hazar dous air pollutant in the Clean Air Act in the USA or reportable compound for pollution release (emission) and transfer (PRTR) in Europe and Japan no information is available about n-PB emissions.

Because emitted n-PB is rapidly destroyed in the lower atmosphere, and therefore does not give rise to significant stratospheric bromine concentrations, its ODP is calculated to be in the range of 0.02-0.1, similar to those of HCFCs.

Proposals to restrict the use of n-PB are based on both ozone-depletion and toxicity
concerns. The American Council of Govern ment Industrial Hygienists (ACGIH) and Israel have set an exposure guideline of 10 ppm, with Europe setting the lowest 8-hour occupational exposure limit (OEL) value in humans and enforcing the tightest labelling classification. The US EPA is proposing to allow n-PB in some, but not all, end uses as a solvent, with a TLV (Threshold Limit Valu e) of 10ppm as an 8-hour time-weighted2010 CTOC Progress Report 16 average of exposure (TWA) through its SNAP (Significant New Alternatives Policy) Program, although OSHA has not yet issued a Permissible Exposure Limit (PEL) for
n-PB.2010 CTOC Progress Report 17 

### 5. Destruction Technologies

5.1 Introduction

Following the discovery of the ozone hole an d establishment of the Montreal Protocol, the first report of the “Ad-Hoc Technica l Advisory Committee on ODS Destruction Technologies” was published in May, 1992.

TEAP was requested to establish two task forces; a task force on collection, recovery and storage and a task force on destruction technologies. Their reports were published in April, 2002. The task for ce on collection, recovery and storage reported (1) technical feasibility of collection, recovery and storage, (2) inventories and collection potential, (3) economic implication, and (4) barrier to collection, recovery and storage. The task force on destruction technologies reported in May, 2002 that the criteria of the destruction were (1) destruction and removal efficiency (DRE), (2) emissions of PCDDs/PCDFs, (3) emissions of acid gases, particulate matter and carbon monoxide, and (4) technical capability (scale of destruction). The task force concluded that sixteen ODS destruction technologies met the scr eening criteria among 45 technologies.

TEAP was requested by Decision XVII/10 to establish the task force on foam end-of-life issues, focusing on handling and destruction of insulation foams and technical and economic aspects of recovery and destruction of blowing agents from appliance and building insulation foams. The report of the task force of collection, recovery and storage in May, 2005, conclude d (1) a new practically-valuable parameter, recovery and destruction efficiency (RDE ), (2) anaerobic degradation of ODS in landfilling, and (3) economic factors affect ed by segregation of foams from other
materials and infrastructure of transport, and (4) estimated banks of CFCs (1.5 million tonnes) and HCFCs (0.75 million tonnes).

The IPCC/TEAP special report in 20 05 described emission scenarios and recovery/destruction of HFCs, PFCs and SF 6 as well as CFCs and HCFCs. A1 scenario of SRES (Special Report on Emission Scenar ios for IPCC Third Assessment Report in 2001) indicated that while global emissions of ODS, HFCs-total and PFCs-total are 842 kt, 93 kt and 14 kt in 2000, respectively, those in 2010 are projected to be 786 kt, 298 kt and 17 kt, respectively. Particularly, the emissions of HFC-23 were 12.6 kt in 2000 and were projected to be 14.8 kt in 2010, and those of HFC-134a were 80.0 kt in
2000 and were to be 175.7 kt in 2010. The special report explained recovery, recycling and reclamation of ODS and HFCs. The repo rt also described the destruction of a by-product of HFC-23, which is produced in HCFC-22 manufacturing by 1.4% to 4% and has a GWP of 14,310.

5.2 Recent Progress

5.2.1 Environmentally Sound Management of Banks of ODS

By Decision XX/7 TEAP was requested to establish the Task Force on “Environmentally Sound Management of Banks of Ozone-depleting Substances.” The Interim report in June, 2009 and Phase 2 report in October, 2009 drew main2010 CTOC Progress Report 18 conclusions. (1) The evaluati on of ODS flow reaching to the waste streams indicated that while opportunity for end-of-life management of ODS, for example, in refrigerant will be over by 2025 in developed countries, the management of CFCs in refrigerant will be over the next 10-15 years and that of HCFC-22 will be prevalent up to 2030 in developing countries. (2) Synergy of ODS with other waste issues indicated importance of integrating ODS into wider waste manageme nt strategies, based on cost analyses of the recovery and destruction which were composed of segregation/collection equipment containing ODS, transport of recovered equipment, recovery of ODS from equipment, transport of recovered ODS to destruction, and destruction of ODS. The synergy of ODS with other waste issues wa s supported by three sub-regional examples in EU, Brazil and Japan. (3) A further colla boration of the ozone, climate and other
environmental benefit indicated annual benefits in excess of 400 Mtonnes of CO 2 -eq were available from management of low and medium effort banks reaching to the

waste stream.

5.2.2 Update of the screened-in destruction technologies of 2002 TF Report

As described in the 2002 TEAP Task Force on Destruction Technologies, only sixteen destruction technologies were screened-in. However, from the documents distributed by the Ozone Secretariat until October 2009, the CTOC identified at least 176 destruction facilities in 27 countries which are being operated. Present destruction facilities are operated by a variety of technologies far wider than the 2002 Task Force technologies. The technologies applied are cl assified into four categories, i.e. high temperature incineration, furnaces dedica ted to manufacturing, plasma, and other
non-incineration.

Furnaces dedicated to manufacturing include ce ment kilns, lime rotary kilns, electric furnace, sulphuric acid recovery furnace and lightweight aggregate kilns. Other non-incineration technologies include catalytic destruction, chemical treatment and solid-phase alkaline reactor. As indicated in the 2002 Task Force report, the suggested minimum standards of technical performance are guidelines for selecting the destruction technologies.

Current destruction technologies other than the sixteen TEAP recommended technologies were evaluated against the perf ormance criteria of their own countries, as well as by those of the 2002 Task Force re port. The United States of America, for instance, has established their domestic technologies permitted by the Resource Conservation and Recovery Act requirements and ODS has been destroyed under MACT (Maximum Achievable Control T echnology) standards for destruction efficiency (DE) and atmospheric emissions. In European countries, ODS is destroyed by the technologies recommended by the 2002 Task Force report and by a variety of incinerators that are used for PCB/POPs destruction. Japan has permitted the destruction technologies based on the Law of Fluorocarbon Recovery and Destruction.

5.2.3 Article 5 countries

CTOC is aware that technology transfer to Article 5 countries has begun take place. The ODS destruction project in Indonesia us ing cement kiln project was supported by2010 CTOC Progress Report 19 the Japanese government and a private comp any. Such assistance to A-5 countries is likely to increase since ODS destruction can be expected to be more emphasized in
such countries.

Since 1993 EU and USA have destroyed 114,603 and 38,278 tonnes of ODS, respectively. Japan has destroyed 25,925 tonnes of CFCs, HCFCs and HFCs. Recently, Korea, China, Brazil and some A-5 countr ies have started destruction of ODS.

The CTOC is also aware that movement of waste ODS from countries where they have been withdrawn from service, but in which no destruction facilities exist, to other countries (sometimes neighbouring countries) where destruction facilities are available, can prove difficult. The Basel Convention applies but there is also reluctance on the part of many countries to accept waste from other countries for destruction.

5.2.4 Evaluation of reported emerging technologies

CTOC has received three kinds of emerging destruction technolo gies for evaluation and recommendation. Although some information about these technologies are confidential, CTOC expects to be able to advise Parties on their technical performance. Appropriate advice has been sent to the in venters regarding technical performance of these technologies and suitable substances to be destroyed under destruction conditions. When detailed technical information is made available, these technologies will be evaluated as requested in Decision XXII/10.

A fourth technical proposal concerns th e applicability of current destruction technologies to methyl bromide (MB). Although MB among ODS is the most difficult to destroy by incineration, annual amounts of MB destruction ranging from year of 1991 to 2003 were reported by USA (May 2009). The amount destroyed in 2002 was 4,713 metric tones. Commercial recapture systems for MB have been developed based on adsorption of MB from treatment containers and chambers on activated carbon. An emerging destruction technology was attempted by contacting MB released from activated carbon with liquid scrubber co ntaining thiosulfate solution. Another technology for MB destruction was attempted by a plasma technology in Australia.

Revision of the Montreal Protocol assessments of destruction technologies is necessary: Firstly, technical guidelines for methyl bromide might be required, since the 2002 Task Force report was limited to CFCs (concentrated and dilute sources) and halons. Secondly, there is a proposed opinion to specify authorised methods for destruction because of current technologies far wider than those in the 2002 Task Force report. Thirdly, current fluorocarbons to be recovered and destroyed are not limited to ODS, since the mobile and stationary air-conditioners, for example, contain HFC-134a and other HFC and HFC blends as well as CFC-11, CFC-12, HCFC-22, and other ODSs. Finally, comprehensive disposal technologies including recovery and destruction are established for products an d equipment containing ODS. Such a view point may also be helpful for Article 5 countries where ODS recovery/destruction facilities are expected to increase in future. Furthermore, technical, economic and legal mechanisms are desired for ODS recovery and destruction in Ar ticle 5 countries.2010 CTOC Progress Report 21 

### 6. Carbon Tetrachloride (CTC) Emissions and Opportunities for Reduction

Following Decision XVI/14, in 2006 CTOC reported estimates of releases of CTC by chemical industry. For confidentiality reason s, exact usage volumes were not available, and in addition it was necessary to estimate releases on the basis of anticipated small percentage losses. Bottom-up estimated emissions were in the range 12,000-17,000 tonnes/year. Working from the measured atmospheric concentration of CTC and estimates of its tropospheric lifetime, however, top-down annual emissions are estimated to be closer to70,000 tonnes/year. Just how this discrepancy could be reconciled is not obvious, but CTOC drew attention to possible under-reporting of CTC use and to uncertainties in the atmospheri c lifetime (with a longer lifetime, lower emissions would suffice to maintain the observed atmospheric concentrations). Decision XVIII/10 requested reconsideration of the matter but in 2007 CTOC reported that their investigations were incomplete. They were able, however, to dismiss the role that landfill emission might play in CTC emissions, and to report that
the Science Assessment Panel had confir med the CTC lifetime (26 years) and suggested regions where unaccounted CTC emis sions might be occurring. In 2008 the TEAP/CTOC reported to the OEWG in Bangkok that SAP emission estimates of 70,000 tonnes/year are inconsistent with re liable estimates of CTC production (200,000 tonnes, including 161,000 tonnes used as fe edstock). There the ma tter rests although there is growing support for the view that, while emissions may be underestimated, the gap is too large to closed unless there is reconsideration of the atmospheric lifetime of
CTC.