GB1592724A - Polycarbonate optical lenses - Google Patents

Polycarbonate optical lenses Download PDF

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Publication number
GB1592724A
GB1592724A GB879/78A GB87978A GB1592724A GB 1592724 A GB1592724 A GB 1592724A GB 879/78 A GB879/78 A GB 879/78A GB 87978 A GB87978 A GB 87978A GB 1592724 A GB1592724 A GB 1592724A
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United Kingdom
Prior art keywords
bisphenol
polycarbonate
mol
lens
lenses
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GB879/78A
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Bayer AG
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Bayer AG
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G64/00Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
    • C08G64/04Aromatic polycarbonates
    • C08G64/06Aromatic polycarbonates not containing aliphatic unsaturation
    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B1/00Optical elements characterised by the material of which they are made; Optical coatings for optical elements
    • G02B1/04Optical elements characterised by the material of which they are made; Optical coatings for optical elements made of organic materials, e.g. plastics
    • G02B1/041Lenses

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  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Lenses (AREA)

Description

(54) POLYCARBONATE OPTICAL LENSES (71) We, BAYER AKTIENGESELLSCHAFT, a body corporate organised under the laws of Germany, of Leverkusen, Germany, do hereby declare the invention for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement:- The invention relates to optical lenses made from an aromatic polycarbonate with relative viscosity 77 rel of 1.20 to 1.60 (measured in CH2Cl2 at 250C) and consisting of 15-100 mol V of structural units of the formula
and 85-0 mol % of structural units of the formula
wherein R denotes
R' denotes -H, -CH3 or -Br, and in particular to high quality lenses for photographic cameras and cinecameras.
The polycarbonate has a refractive index nd of 1.59-1.66, preferably 1.60 1.66, an Able' number vd=29-22, preferably 27.5-22, and a colour triplet of 5.1; 0.1; 0, calculated according to DIN 4,522 part 5.
Optical systems, for example lenses for photographic cameras, have already been manufactured from transparent plastics. Only thermoplastic plastics are important in practice, because they can be processed economically and considerably better than glass. Thus, for example, polymethylmethacrylate is employed instead of silicate glasses of low refractive index. Polystyrene, copolymers of styrene and bisphenol A polycarbonate can also be used, predominantly for dispersing lenses.
The plastics mentioned can only be used for: a) multi-lens objectives consisting only of plastic lenses, with a maximum relative aperture ratio 1:8, a maximum dispersion range < 0.04 mm at 230C/50V relative humidity and a temperature gradient of the focal length 6f mm > 0.008 degree and b) multi-lens objectives with at least one glass lens and 2 to 4 plastic lenses, with a maximum relative aperture ratio 1:5.6, maximum dispersion range < 0.04 mm at 23"C/50% relative humidity, and a temperature gradient of the focal length sf mm > 0.002 degree Because of their low speed, these objectives can only be used with favourable light conditions.
Furthermore, organic polymers are known which have a refractive index fld > 1.59, such as, for example, polycarbodiimides, polybenzimidazoles, polyvinylcarbazole and specific polycarbonates. These products cannot be employed for optical instruments because they are either coloured themselves or cannot be processed thermoplastically or cannot be prepared in a high-molecular weight form.
The polycarbonates for use according to the invention tend not to have these deficiencies, so that optical systems can be manufactured from them which have significant advantages compared with the state of the art. Examples of these advantages are: 1. Better correctability of the image formation errors with larger radii for the lens surfaces (making manufacture easier).
2. Increase in the relative aperture ratio with unchanged dispersion range.
3. Improved resolution by reducing the dispersion range with an unchanged relative aperture ratio.
4. Reduction of the temperature gradients in objectives furnished only with plastic lenses and in objectives furnished with glass lenses and plastic lenses.
5. Manufacture of lens systems with relative aperture ratios above 1:8 consisting only of plastic lenses.
Polycarbonates which are suitable for making lenses according to the invention are those consisting of 15-100 mol V of structural units of the formula
and 85-0 mol V of structural units of the formula
wherein R denotes
R' denotes -H, -CIl3 or -Br, Those in which the structural unit II corresponds to the formula
are preferred and those which are built up from 35-50 mol V of structural units I and 65-50 mol V of structural units II are particularly preferred.
These polycarbonates fulfil the mechanical and thermal requirements placed on an optical material. They can be processed thermoplastically without impairing the mechanical and optical properties. They retain their shape under the influence of heat up to at least 900 C, possess a good impact strength, low shrinkage during processing, low coefficient of expansion, low weight, low absorption of water, good flow behaviour, good mould-release properties, good resistance to ageing and a colour triplet of 5.1; 0.1; 0, calculated according to DIN 4,522 part 5. Stabilisers, UV absorbers, mould-releasing agents and antistatic agents can be incorporated without impairing these properties.
The polycarbonates can be prepared by known processes; for example by the melt trans-esterification process from bisphenol and diphenyl carbonate, and the two phase boundary process from bisphenols and phosgene.
The melt trans-esterification process is preferably used for polycarbonates with more than 50 mol V of structural units I because they are sparingly soluble.
Otherwise, the two phase boundary process, which is briefly described in the following, is preferred.
The bisphenols are dissolved in aqueous alkali, preferably in sodium hydroxide solution or potassium hydroxide solution, and a solvent which is suitable for the polycarbonate formed is added. Suitable solvents are, in general, chlorohydrocarbons, such as methylene chloride, chloroform and 1,2dichloroethane, but also chlorinated aromatic compounds, such as chlorobenzene, dichlorobenzene and chlorotoluene. Phosgene is passed into this mixture, whilst stirring vigorously.
In the case of bisphenols which, because of their hydrophobic character, give no bisphenolate solutions, a suspension is advantageously used.
The phosgenation required depends on the bisphenol employed, the stirring effect and the reaction temperature, which can be between about 10 and about 60"C, and in general is 1.1 to 3.0 mols of phosgene per mol of bisphenol.
After the phosgenation, which can also already be carried out in the presence of chain stoppers, for example phenol or substituted monophenols, the condensation reaction to give a high-molecular polycarbonate is then carried out by adding a tertiary amine, for example triethylamine, dimethylbenzylamine or triethylenediamine, as a catalyst. In general, the amounts of amine are 1 to 10 mol V relative to bisphenol, but 2 to 10 mol V are preferably used; in general, a reaction time of about 0.5 to about 1.5 hours is sufficient.
The polycarbonates can be branched by incorporating small amounts, preferably amounts between 0.05 and 2.0 mol V (relative to diphenols employed), of compounds which are tri-functional or more than tri-functional, in particular those with three or more than three phenolic hydroxyl groups.
The polycarbonates thus prepared can be isolated by known processes, for example by separating off the aqueous phase, washing the organic phase several times with water until free from electrolyte and thereafter precipitating the polycarbonate or evaporating off the solvent. The polycarbonates thus obtained contain no portions of saponifiable chlorine.
The yields are virtually quantitative.
Another preparation process is polycondensation in a homogeneous phase. In this process, the hydroxy compounds to be used are dissolved in an inert solvent, such as, for example, methylene chloride, with the addition of an equivalent amount of a tertiary base, such as, for example, N,N-dimethylaniline, dimethylcyclohexylamine or, preferably, pyridine. The polycondensation reaction is then carried out by passing in gaseous derivatives of carbonic acid or by adding solutions of liquid or solid derivatives of carbonic acid dropwise.
The chlorocarbonic acid esters of monovalent or more than divalent phenols can also be used in the processes described.
As mentioned above, it is also possible to obtain the polycarbonates for use in the invention by trans-esterification according to the melt polycondensation process.
For this, the bisphenols are advantageously reacted with diphenylcarbonate under an inert gas atmosphere in the presence of alkaline catalysts, such as, for example, oxides, hydroxides, carbonates, hydrides and phenolates of alkali metals and alkaline earth metals, at temperatures rising from 200 to 3600 C, preferably 240 to 3000C and under a pressure which is gradually reduced to 20-1 mm Hg and the phenol liberated during the reaction is continuously distilled off. The polymer formed is directly extruded and granulated.
A considerable advantage of the polycarbonates used in the invention is that the refractive index and optical dispersion of the materials can be determined freely, within certain limits. by the nature and amount of the co-condensed comonomers. New possibilites in the calculation and realisation of optical systems are thereby opened up.
Optical lenses can be manufactured from the polycarbonates in the customary manner by injection moulding. The resulting injection-moulded articles can be employed without further processing. The polycarbonates are essentially used for the manufacture of lenses and lens systems for cameras.
Example 1 Copolycarbonate of bisphenol A and bisphenol S xt 40.0 g (1 mol) of NaOH are dissolved in 600 ml of water, and 39.8 g (0.17 mol) of bisphenol A, 6.54 g (0.03 mol) of bisphenol S, 1.02 g (0.0068 mol) of p-tert.butylphenol and 600 ml of CH2Cl2 are then added, whilst stirring. 29.7 g (0.3 mol) of phosgene are passed in, whilst stirring vigorously. 2 ml of a 3V strength triethylamine solution are then added and the mixture is stirred vigorously for a further 90 minutes. The entire reaction is carried out under nitrogen and at 20 to 25"C. After the further stirring, the mixture is worked up. The aqueous phase is free from bisphenol. The organic phase is diluted with 1,000 ml of CH2CI2 and washed with 100 ml of 20% strength aqueous phosphoric acid and then with water until free from electrolyte. After concentrating the organic phase to 600 ml, this is added dropwise to 2,500 ml of methanol, whereupqn the polycarbonate precipitates. It is dried. The yield of white, flocculent polycarbonate is 44 g. The relative viscosity of the polycarbonate is 1.278 (in CH2CI2 at 250C, C=5 g/l).
Colourless, clear tough films can be drawn from the methylene chloride solution of the polymer. The optical data, measured on a film, are: n,=1.5929 vd=28.9.
x) 4,4'-dihydroxydiphenyl sulphide; 4,4'-thiodiphenol.
Example 2 Copolycarbonate of bisphenol A and bisphenol S The procedure followed is according to Example 1 and, with a molar ratio of bisphenol A: bisphenol S=50:50, a colourless product with a relative viscosity 17rev of 1.282 (in CH2Cl2 at 25"C C=5 girl) is obtained. The optical data measured on a film are: no=1.6148 vd=25.6.
Example 3 Copolycarbonate of bisphenol A and bisphenol S x} 2,500 g (62.5 mols of NaOH are dissolved in 35 1 of water, and 1,710 g (7.5 mols) of bisphenol A, 1,090 g (5.0 mols) of bisphenol S. 75.11 g (0.5 mol) of p-tert.butylphenol and 2 g of NaB H4 are added to the solution, whilst stirring. After adding 351 of CH2CI2, 1,732 g (17.5 mols) of phosgene are passed in at 20 to 250C.
12.1 g of triethylamine are then added and the mixture is stirred for a further 60 minutes. The organic phase is washed twice with 2V strength phosphoric acid and then with water until free from electrolyte. The methylene chloride is evaporated off. The resulting polymer is comminuted, and dried for 48 hours in vacuo at 120"C. 2,630 g of a colourless product with a relative viscosity 71rev of 1.245 (in CH2CI2, 25"C, C=5 girl) and a glass transition temperature of 132"C is obtained.
After adding 0.5V by weight of a UV absorber, the material is extruded at 2700 C.
The colourless granules are processed to injection-moulded articles; optical data; n,-1.61289; vd=26. I .
Example 4 Polycarbonate of bisphenol S x} 87.2 g (0.4 mol) of bisphenol S are mixed with 94.1 g (0.44 mol) of diphenylcarbonate, and 25 mg of a mixture of sodium bisphenolate and bisphenol A (1:99) are added as the catalyst. The mixture is heated, whilst stirring. In the course of 5 hours, the temperature is increased from 220"C to 3000C and the pressure is reduced to a final value of I mm Hg. During this procedure, the phenol liberated distils off. After cooling the melt, the resulting polycarbonate is comminuted and moulded into test pieces by Injection. Optical data: no=1.6577; vd=22. 1.
x) 4,4'-dihydroxydiphenylsulphide; 4,4'-thiodiphenol.
Example 5 Copolycarbonate of bisphenol S x} and 4,4'-dihydroxytetraphenylmethane The procedure followed is according to Example 1 and, with a ratio of 60 mol V of 4,4'-dihydroxytetraphenylmethane and 40 mol V of bisphenol S, 30 g of a colourless product with a relative viscosity of 1.224 (in CH2CI2 at 250C, C=5 girl) are obtained. The optical data, measured on a film, are: nd=1.63677; vd=25.4.
x) 4,4'-dihydroxydiphenyl sulphide, 4,4'-thiodiphenol.
EXAMPLE 6 The radii changes of a 3 lens objective were calculated using the optical data of the material from Example 4. It was assumed that a version exists as substantially shown and described in the drawing comprised of a glass lens (LaF2), a lens of bisphenol A-polycarbonate and a lens of PMMA (polymethyl-methacrylate) of the following values: Lens Material nd vd Vd L, LaF2 1.7440 44.77 L2 PC of bisphenol-A 1.5858 30.0 L3 PMMA 1.491 58.0 The measurements for lens 2 are: L2 r3=-32.478 r4= +6.287 d2= 0.860 When replacing the lens of polycarbonate (lens 2) with the material used in Example 4, the following measurements result: L2, r13=-36.462 r'4= +7.058 d'2= 0.899 All other measurements of lenses 1 and 3 as well as the air distance 11 and 12 remained unchanged.
The focal distance of f=26.8 mm, the relative opening of 1:6.45, and the quality requirements (circle of divergence < 0.02 mm near the axis) remained unchanged.
WHAT WE CLAIM IS: 1. Optical lenses made from an aromatic polycarbonate with a relative viscosity free of 1.20 to 1.60 (measured in CH2Cl2 at 250C) consisting of 15-100 mol V of structural units of the formula
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (9)

**WARNING** start of CLMS field may overlap end of DESC **. 12.1 g of triethylamine are then added and the mixture is stirred for a further 60 minutes. The organic phase is washed twice with 2V strength phosphoric acid and then with water until free from electrolyte. The methylene chloride is evaporated off. The resulting polymer is comminuted, and dried for 48 hours in vacuo at 120"C. 2,630 g of a colourless product with a relative viscosity 71rev of 1.245 (in CH2CI2, 25"C, C=5 girl) and a glass transition temperature of 132"C is obtained. After adding 0.5V by weight of a UV absorber, the material is extruded at 2700 C. The colourless granules are processed to injection-moulded articles; optical data; n,-1.61289; vd=26. I . Example 4 Polycarbonate of bisphenol S x} 87.2 g (0.4 mol) of bisphenol S are mixed with 94.1 g (0.44 mol) of diphenylcarbonate, and 25 mg of a mixture of sodium bisphenolate and bisphenol A (1:99) are added as the catalyst. The mixture is heated, whilst stirring. In the course of 5 hours, the temperature is increased from 220"C to 3000C and the pressure is reduced to a final value of I mm Hg. During this procedure, the phenol liberated distils off. After cooling the melt, the resulting polycarbonate is comminuted and moulded into test pieces by Injection. Optical data: no=1.6577; vd=22. 1. x) 4,4'-dihydroxydiphenylsulphide; 4,4'-thiodiphenol. Example 5 Copolycarbonate of bisphenol S x} and 4,4'-dihydroxytetraphenylmethane The procedure followed is according to Example 1 and, with a ratio of 60 mol V of 4,4'-dihydroxytetraphenylmethane and 40 mol V of bisphenol S, 30 g of a colourless product with a relative viscosity of 1.224 (in CH2CI2 at 250C, C=5 girl) are obtained. The optical data, measured on a film, are: nd=1.63677; vd=25.4. x) 4,4'-dihydroxydiphenyl sulphide, 4,4'-thiodiphenol. EXAMPLE 6 The radii changes of a 3 lens objective were calculated using the optical data of the material from Example 4. It was assumed that a version exists as substantially shown and described in the drawing comprised of a glass lens (LaF2), a lens of bisphenol A-polycarbonate and a lens of PMMA (polymethyl-methacrylate) of the following values: Lens Material nd vd Vd L, LaF2 1.7440 44.77 L2 PC of bisphenol-A 1.5858 30.0 L3 PMMA 1.491 58.0 The measurements for lens 2 are: L2 r3=-32.478 r4= +6.287 d2= 0.860 When replacing the lens of polycarbonate (lens 2) with the material used in Example 4, the following measurements result: L2, r13=-36.462 r'4= +7.058 d'2= 0.899 All other measurements of lenses 1 and 3 as well as the air distance 11 and 12 remained unchanged. The focal distance of f=26.8 mm, the relative opening of 1:6.45, and the quality requirements (circle of divergence < 0.02 mm near the axis) remained unchanged. WHAT WE CLAIM IS:
1. Optical lenses made from an aromatic polycarbonate with a relative viscosity free of 1.20 to 1.60 (measured in CH2Cl2 at 250C) consisting of 15-100 mol V of structural units of the formula
and 854 mol V of structural units of the formula
wherein R denotes
R' denotes -H, CH3 or -Br.
2. Lenses according to claim 1 wherein R is
and R' is -H.
3. Lenses according to claim I or 2 wherein the polycarbonate consists of 3550 mol V of structural units I and 65-50 mol V of structural units 11.
4. Lenses according to any one of claims 1 to 3 wherein the polycarbonate includes a stabiliser, U.V. absorber, mould release agent or anti-static agent.
5. Lenses according to any one of claims 1 to 4 wherein the polycarbonate is prepared by a melt trans-esterification process from a bisphenol and diphenyl carbonate, or by a two phase boundary process from a bisphenol and phosgene.
6. Lenses according to any one of claims 1 to 4 wherein the polycarbonate is prepared by polycondensation in a homogeneous phase.
7. Lenses according to any one of claims 1 to 6, for cameras.
8. An aromatic polycarbonate, when used for making optical lenses as defined in claim 1, substantially as hereinbefore described in any of Examples I to 5.
9. Optical lenses as claimed in claim I, substantially as hereinbefore described in Example 6 and with reference to the accompanying drawing.
GB879/78A 1977-01-13 1978-01-10 Polycarbonate optical lenses Expired GB1592724A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2701173A DE2701173C2 (en) 1977-01-13 1977-01-13 Use of polycarbonates to manufacture lenses for photo and film cameras

Publications (1)

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GB1592724A true GB1592724A (en) 1981-07-08

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JP (1) JPS5389752A (en)
DE (1) DE2701173C2 (en)
FR (1) FR2377267A1 (en)
GB (1) GB1592724A (en)
IT (1) IT1104626B (en)
NL (1) NL186143C (en)

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US6180698B1 (en) 1997-02-28 2001-01-30 Candescent Technologies Corporation Polycarbonate-containing liquid chemical formulation and method for making polycarbonate film
US6500885B1 (en) 1997-02-28 2002-12-31 Candescent Technologies Corporation Polycarbonate-containing liquid chemical formulation and methods for making and using polycarbonate film
US7169333B2 (en) 2000-05-12 2007-01-30 Bayer Aktiengesellschaft Antistatic agent
US7425358B2 (en) 2004-05-07 2008-09-16 Bayer Materialscience Ag Copolycarbonates having improved flowability
US7847051B2 (en) 2008-03-05 2010-12-07 Bayer Materialscience Ag Phase boundary processes for preparing polycarbonates
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US7968671B2 (en) 2008-05-15 2011-06-28 Bayer Material Science Ag Alkylphenol-terminated copolycarbonates, processes for preparing the same, molding compositions containing the same, and articles prepared therefrom
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GB2141556A (en) * 1983-06-14 1984-12-19 Pilkington Perkin Elmer Ltd Glass and plastics objective lens for low light level viewing apparatus
US6180698B1 (en) 1997-02-28 2001-01-30 Candescent Technologies Corporation Polycarbonate-containing liquid chemical formulation and method for making polycarbonate film
US6500885B1 (en) 1997-02-28 2002-12-31 Candescent Technologies Corporation Polycarbonate-containing liquid chemical formulation and methods for making and using polycarbonate film
US7169333B2 (en) 2000-05-12 2007-01-30 Bayer Aktiengesellschaft Antistatic agent
US7425358B2 (en) 2004-05-07 2008-09-16 Bayer Materialscience Ag Copolycarbonates having improved flowability
US7879967B2 (en) 2007-04-03 2011-02-01 Bayer Materialscience Ag Modified polycarbonates, polyester carbonates and polyesters having improved elongation behavior and flame resistance
US8202961B2 (en) 2008-02-13 2012-06-19 Bayer Materialscience Ag Alkylphenol for adjusting the molecular weight, and polycarbonate compositions having improved properties
US8110649B2 (en) 2008-02-29 2012-02-07 Bayer Materialscience Ag Polycarbonates comprising cyclic oligomers and having an improved flow behavior
US7847051B2 (en) 2008-03-05 2010-12-07 Bayer Materialscience Ag Phase boundary processes for preparing polycarbonates
US8158745B2 (en) 2008-04-18 2012-04-17 Bayer Materialscience Ag Polycarbonates having rearrangement structures, cyclic and linear oligomers and also flow behavior
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US8329852B2 (en) 2008-11-28 2012-12-11 Bayer Materialscience Ag Copolycarbonates having improved surface hardness
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US9139730B2 (en) 2009-03-26 2015-09-22 Bayer Materialscience Ag (Co)polycarbonates with improved optical properties
US9771451B2 (en) 2014-01-24 2017-09-26 Covestro Deutschland Ag Method for producing polycarbonate according to the phase interface method
US11326018B2 (en) 2016-08-19 2022-05-10 Covestro Deutschland Ag Process for the synthesis of polyoxazolidinone compounds
US11319398B2 (en) 2017-02-02 2022-05-03 Covestro Deutschland Ag Method for the production of polyoxazolidinone polymer compounds

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JPS5389752A (en) 1978-08-07
FR2377267A1 (en) 1978-08-11
FR2377267B1 (en) 1983-07-01
NL186143C (en) 1990-10-01
NL186143B (en) 1990-05-01
IT7847588A0 (en) 1978-01-11
IT1104626B (en) 1985-10-21
NL7800292A (en) 1978-07-17
DE2701173C2 (en) 1983-02-10
DE2701173A1 (en) 1978-07-20

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