natgillin/translations-raw huggingface dataset:
For industrial boilers and district heating plants put into operation no later than 27 November 2003 and operated < 1500 h/yr, the higher end of the BAT-AEL range is 400 mg/Nm3.
V CCGT sa teplo zo spalín plynovej turbíny (fungujúcej podľa Braytonovho cyklu na výrobu elektriny) premieňa na využiteľnú energiu v spalinovom kotli (heat recovery steam generator, HRSG), kde sa využíva na výrobu pary, ktorá potom expanduje v parnej turbíne (fungujúcej podľa Rankinovho cyklu na výrobu ďalšej elektriny).
The higher end of the BAT-AEL range is 175 mg/Nm3 for plants put into operation no later than 7 January 2014.
Chemická spotreba kyslíka Množstvo kyslíka potrebné na celkovú oxidáciu organickej hmoty na oxid uhličitý
For industrial boilers and district heating plants put into operation no later than 27 November 2003, which are operated < 1500 h/yr and for which wet FGD is not applicable, the higher end of the BAT-AEL range is 200 mg/Nm3.
Čistá elektrická účinnosť (%) [39]
The higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014.
100 – 150
The higher end of the BAT-AEL range is 15 mg/Nm3 for plants put into operation no later than 7 January 2014.
100 – 270
As defined in point 26 of Article 2 of Directive 2009/72/EC.
155 – 200
As defined in point 27 of Article 2 of Directive 2009/72/EC.
165 – 330
Net electrical efficiency BAT-AEELs apply to CHP units whose design is oriented towards power generation, and to units generating only power.
50 – 100
These levels may be difficult to achieve in the case of engines fitted with energy-intensive secondary abatement techniques.
100 – 180
This level may be difficult to achieve in the case of engines using a radiator as a cooling system in dry, hot geographical locations.
80 – 130
These BAT-AELs do not apply to plants operated < 1500 h/yr or to plants that cannot be fitted with secondary abatement techniques.
155 – 210
The BAT-AEL range is 1150–1900 mg/Nm3 for plants operated < 1500 h/yr and for plants that cannot be fitted with secondary abatement techniques.
< 30 – 140
For plants including units of < 20 MWth combusting HFO, the higher end of the BAT-AEL range applying to those units is 225 mg/Nm3.
< 30 – 100 [55]
These BAT-AELs do not apply to plants operated < 1500 h/yr.
< 5 – 100 [55]
The higher end of the BAT-AEL range is 280 mg/Nm3 if no secondary abatement technique can be applied.
2 – 8
This corresponds to a sulphur content of the fuel of 0,5 wt-% (dry).
Čistá elektrická účinnosť (%) [76]
These BAT-AELs do not apply to existing plants operated < 1500 h/yr.
70 – 150 [82]
For existing plants operated < 500 h/yr, these levels are indicative.
70 – 225 [83]
In the case of CHP units, only one of the two BAT-AEELs ‘Net electrical efficiency’ or ‘Net total fuel utilisation’ applies, depending on the CHP unit design (i.e. either more oriented towards electricity generation or heat generation).
120 – 200 [84]
Net total fuel utilisation BAT-AEELs may not be achievable if the potential heat demand is too low.
120 – 275 [85]
These BAT-AEELs apply to units used for mechanical drive applications.
100 – 300
These levels may be difficult to achieve in the case of engines tuned in order to reach NOX levels lower than 190 mg/Nm3.
50 – 140
These BAT-AELs also apply to the combustion of natural gas in dual-fuel-fired turbines.
50 – 180
In the case of a gas turbine equipped with DLN, these BAT-AELs apply only when the DLN operation is effective.
100 – 200
Optimising the functioning of an existing technique to reduce NOX emissions further may lead to levels of CO emissions at the higher end of the indicative range for CO emissions given after this table.
100 – 220
These BAT-AELs do not apply to existing turbines for mechanical drive applications or to plants operated < 500 h/yr.
40 – 140
For plants with a net electrical efficiency (EE) greater than 39 %, a correction factor may be applied to the higher end of the range, corresponding to [higher end] × EE/39, where EE is the net electrical energy efficiency or net mechanical energy efficiency of the plant determined at ISO baseload conditions.
40 – 150 [86]
The higher end of the range is 80 mg/Nm3 in the case of plants which were put into operation no later than 27 November 2003 and are operated between 500 h/yr and 1500 h/yr.
65 – 150
For plants with a net electrical efficiency (EE) greater than 55 %, a correction factor may be applied to the higher end of the BAT-AEL range, corresponding to [higher end] × EE/55, where EE is the net electrical efficiency of the plant determined at ISO baseload conditions.
95 – 165 [87]
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 55 mg/Nm3.
15 – 100
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 80 mg/Nm3.
30 – 175
The lower end of the BAT-AEL range for NOX can be achieved with DLN burners.
30 – 215
These levels are indicative.
< 10 – 50
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 60 mg/Nm3.
< 10 – 70 [90]
These BAT-AELs only apply to spark-ignited and dual-fuel engines.
< 20 – 85
They do not apply to gas-diesel engines.
< 20 – 175 [91]
In the case of engines for emergency use operated < 500 h/yr that could not apply the lean-burn concept or use SCR, the higher end of the indicative range is 175 mg/Nm3.
< 10 – 35
For existing plants operated < 500 h/yr, these levels are indicative.
< 10 – 50 [90]
This BAT-AEL is expressed as C at full load operation.
< 20 – 70
The wide range of energy efficiencies in CHP units is largely dependent on the local demand for electricity and heat.
< 20 – 85 [92]
These BAT-AEELs do not apply in the case of units operated < 1500 h/yr.
Čistá elektrická účinnosť (%) [121]
Plants combusting a mixture of gases with an equivalent LHV of > 20 MJ/Nm3 are expected to emit at the higher end of the BAT-AEL ranges.
Čistá elektrická účinnosť (%) [134]
The lower end of the BAT-AEL range can be achieved when using SCR.
Neuplatňujú sa na spaľovacie zariadenia na morských plošinách; tých sa týka oddiel 4.3.
For plants operated < 1500 h/yr, these BAT AELs do not apply.
Existujúce OCGT s príkonom ≥ 50 MWth (okrem turbín na účely mechanického pohonu): < 5 – 40 mg/Nm3.
In the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 160 mg/Nm3.
Horná hranica tohto rozsahu bude vo všeobecnosti 80 mg/Nm3 v prípade existujúcich zariadení, ktoré nemôžu byť vybavené suchými technikami na zníženie NOX, alebo 50 mg/Nm3 v prípade zariadení, ktoré sa prevádzkujú pri nízkom zaťažení.
Furthermore, the higher end of the BAT-AEL range may be exceeded when SCR cannot be used and when using a high share of COG (e.g. > 50 %) and/or when combusting COG with a relatively high level of H2.
25 – 150
In this case, the higher end of the BAT-AEL range is 220 mg/Nm3.
50 – 200 [180]
In the case of plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 70 mg/Nm3.
10 – 45
For existing plants operated < 1500 h/yr, these BAT AELs do not apply.
20 – 70
The higher end of the BAT-AEL range may be exceeded when using a high share of COG (e.g. > 50 %).
Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V (mg/Nm3)
In this case, the higher end of the BAT-AEL range is 300 mg/Nm3.
Tieto BAT-AEL sa uplatňujú iba na zážihové a dvojpalivové motory.
For existing plants operated < 1500 h/yr, these BAT-AELs do not apply.
Neuplatňujú sa na plynovo-dieselové motory.
For existing plants operated < 500 h/yr, these levels are indicative
Séria referenčných dokumentov o BAT týkajúcich sa chemických látok (LVOC atď.)
These BAT-AELs are based on > 70 % of baseload power available on the day.
Hospodárska únosnosť a medzizložkové vplyvy (Economics and Cross-Media Effects, ECM)
This includes single fuel and dual fuel gas turbines.
Emisie zo skladovania (Emissions from Storage, EFS)
The higher end of the BAT-AEL range is 250 mg/Nm3 if DLN burners are not applicable.
150 – 200
The lower end of the BAT-AEL range can be achieved with DLN burners.
150 – 360
In the case of CHP units, only one of the two BAT-AEELs ‘Net electrical efficiency’ or ‘Net total fuel utilisation’ applies, depending on the CHP unit design (i.e. either more oriented towards generation electricity or towards heat generation).
170 – 220
These BAT-AEELs may not be achievable if the potential heat demand is too low.
170 – 400
For existing plants of ≤ 500 MWth put into operation no later than 27 November 2003 using liquid fuels with a nitrogen content higher than 0,6 wt-%, the higher end of the BAT-AEL range is 380 mg/Nm3.
80 – 150
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 180 mg/Nm3.
95 – 200
For existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 210 mg/Nm3.
135 – 200
In the case of plants operated < 1500 h/yr, the higher end of the BAT-AEL range is 20 mg/Nm3.
135 – 220 [58]
For plants operated < 1500 h/yr, these BAT-AELs do not apply.
10 – 130 [59]
For plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 25 mg/Nm3.
25 – 110
For plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 15 mg/Nm3.
25 – 165 [60]
These BAT-AELs only apply to plants using fuels derived from chemical processes involving chlorinated substances.
20 – 75
Monitoring of Emissions to Air and Water from IED installations (ROM)
2 – 10 [63]
Production of Pulp, Paper and Board (PP)
1 – 5 [63] [64]
A CCGT is a combustion plant where two thermodynamic cycles are used (i.e. Brayton and Rankine cycles).
< 1 – 3
In a CCGT, heat from the flue-gas of a gas turbine (operating according to the Brayton cycle to produce electricity) is converted to useful energy in a heat recovery steam generator (HRSG), where it is used to generate steam, which then expands in a steam turbine (operating according to the Rankine cycle to produce additional electricity).
< 1 – 6 [65]
Chemical oxygen demand.
< 1 – 2
Amount of oxygen needed for the total oxidation of the organic matter to carbon dioxide
< 1 – 3 [65]
Polychlorinated dibenzo-p-dioxins and -furans RCG
2 – 5
Recovery of heat (mainly from the steam system) for producing hot water/steam to be used in industrial processes/activities or in a public network for district heating.
2 – 18
Additional heat recovery is possible from:
4 – 16
Net electrical efficiency (%) [39]
4 – 22 [68]
100–150
2 – 14
100–270
4 – 22 [69]
155–200
300 – 1000
50–100
3 – 10
100–180
3 – 11 [71]
80–130
3 – 11 [72]
155–210
< 1 – 5
< 30–140
< 1 – 9
< 30–100 [55]
< 1 – 10
< 5–100 [55]
< 1 – 4
2–8
< 1 – 7
BAT conclusions for the combustion of solid biomass and/or peat Unless otherwise stated, the BAT conclusions presented in this section are generally applicable to the combustion of solid biomass and/or peat.
28 – 38
Net electrical efficiency (%) [76]
73 – 99
70–150 [82]
2 – 15
70–225 [83]
2 – 10
120–200 [84]
2 – 22
120–275 [85]
2 – 12
100–300
2 – 16
50–140
35,6 – 37,4
50–180
80 – 96
100–200
75 – 200
100–220
150 – 270
40–140
100 – 215
40–150 [86]
210 – 33 [105]
65–150
45 – 75
95–165 [87]
45 – 100 [106]
15–70
85 – 100
15–100
85 – 110 [107] [108]
30–175
50 – 175
30–215
150 – 200 [111]
< 10–50
35 – 50
< 10–70 [90]
50 – 110
< 20–85
50 – 120
< 20–175 [91]
150 – 165 [112] [113]
< 10–35
2 – 20
< 10–50 [90]
7 – 18
< 20–70
7 – 22 [116]
< 20–85 [92]
7 – 10
Net electrical efficiency (%) [121]
7 – 11 [117]
They do not apply to combustion plants on offshore platforms; these are covered by Section.
38,3 – 44,5 [122]
Existing OCGT of ≥ 50 MWth (excluding turbines for mechanical drive applications): < 5–40 mg/Nm3.
115 – 190 [127]
The higher end of this range will generally be 80 mg/Nm3 in the case of existing plants that cannot be fitted with dry techniques for NOX reduction, or 50 mg/Nm3 for plants that operate at low load.
125 – 625
25–150
145 – 300
In order to improve the general environmental performance of combustion plants and to reduce emissions to air of CO and unburnt substances, BAT is to ensure optimised combustion and to use an appropriate combination of the techniques given below.
33,5 – 41
BAT 7.
53 – 58,5
In order to reduce emissions of ammonia to air from the use of selective catalytic reduction (SCR) and/or selective non-catalytic reduction (SNCR) for the abatement of NOX emissions, BAT is to optimise the design and/or operation of SCR and/or SNCR (e.g. optimised reagent to NOX ratio, homogeneous reagent distribution and optimum size of the reagent drops).
46 – 54
BAT 8.
57 – 60,5
In order to prevent or reduce emissions to air during normal operating conditions, BAT is to ensure, by appropriate design, operation and maintenance, that the emission abatement systems are used at optimal capacity and availability.
50 – 60
BAT 9.
65 – 95
In order to improve the general environmental performance of combustion and/or gasification plants and to reduce emissions to air, BAT is to include the following elements in the quality assurance/quality control programmes for all the fuels used, as part of the environmental management system (see BAT 1):
15 – 35
BAT 10.
25 – 50
In order to reduce emissions to air and/or to water during other than normal operating conditions (OTNOC), BAT is to set up and implement a management plan as part of the environmental management system (see BAT 1), commensurate with the relevance of potential pollutant releases, that includes the following elements:
15 – 50
BAT 11.
25 – 55 [149]
BAT is to appropriately monitor emissions to air and/or to water during OTNOC.
10 – 30
BAT 12.
15 – 40
In order to increase the energy efficiency of combustion, gasification and/or IGCC units operated ≥ 1500 h/yr, BAT is to use an appropriate combination of the techniques given below.
10 – 40
BAT 13.
18 – 50
In order to reduce water usage and the volume of contaminated waste water discharged, BAT is to use one or both of the techniques given below.
10 – 50
BAT 14.
18 – 55 [151]
In order to prevent the contamination of uncontaminated waste water and to reduce emissions to water, BAT is to segregate waste water streams and to treat them separately, depending on the pollutant content.
50 – 600
BAT 15.
35 – 55
In order to reduce emissions to water from flue-gas treatment, BAT is to use an appropriate combination of the techniques given below, and to use secondary techniques as close as possible to the source in order to avoid dilution.
25 – 50 [152]
BAT 16.
35 – 55 [153]
In order to reduce the quantity of waste sent for disposal from the combustion and/or gasification process and abatement techniques, BAT is to organise operations so as to maximise, in order of priority and taking into account life-cycle thinking:
60 – 140 [154] [155]
In order to reduce noise emissions, BAT is to use one or a combination of the techniques given below.
25 – 55 [157]
BAT 18.
10 – 60
In order to improve the general environmental performance of the combustion of coal and/or lignite, and in addition to BAT 6, BAT is to use the technique given below.
30 – 85
BAT 19.
85 – 110
In order to increase the energy efficiency of the combustion of coal and/or lignite, BAT is to use an appropriate combination of the techniques given in BAT 12 and below.
20 – 100
BAT 20.
55 – 85
In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.
55 – 110 [162]
BAT 21.
5 – 15 [163]
In order to prevent or reduce SOX, HCl and HF emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.
215 – 500 [164]
150–200
215 – 560 [163] [164]
150–360
30 – 40
170–400
36 – 42,5
80–150
40 – 48
95–200
60 – 82
135–200
15 – 65
135–220 [58]
22 – 100
10–75
20 – 100 [173] [174]
10–130 [59]
22 – 110 [173] [175] [176]
20–180
30 – 55 [176] [177]
50–220
2 – 7
2–10 [63]
15 – 50 [185]
1–5 [63] [64]
< 50 – 350 [186]
< 1–3
80 – 290 [193]
< 1–2
20 – 80
< 1–3 [65]
70 – 100 [194]
In order to reduce dust and particulate-bound metal emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.
85 – 110 [195]
2–5
10 – 110
2–18
90 – 200
4–16
2 – 15 [199]
4–22 [68]
< 1 – 6 [200]
2–14
1 – 9 [199]
4–22 [69]
< 1 – 3 [200]
300–1000
2 – 22 [203]
3–10
2 – 11 [203]
3–11 [71]
< 0,012 – 0,036
3–11 [72]
0,6 – 12
BAT 23.
Cd + Tl (μg/Nm3)
In order to prevent or reduce mercury emissions to air from the combustion of coal and/or lignite, BAT is to use one or a combination of the techniques given below.
0,005 – 0,5
< 1–5
5 – 12
< 1–10
5 – 6
< 1–4
0,075 – 0,3
< 1–7
< 0,01 – 0,03
28–38
< 0,1 – 5
73–99
0,5 – 10
BAT 24.
34 – 46
In order to prevent or reduce NOX emissions to air while limiting CO and N2O emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below.
10 – 25
BAT 26.
Použiteľnosť
In order to reduce dust and particulate-bound metal emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below.
Použitie spaľovacieho vzduchu pri teplote okolia Spaľovací vzduch sa nepredhrieva v rekuperačnom predhrievači vzduchu.
2–15
Použiteľné všeobecne na nové zariadenia V existujúcich zariadeniach môže byť vloženie prekážok obmedzené nedostatkom miesta.
2–10
Použiteľné všeobecne na nové zariadenia V existujúcich zariadeniach môže byť premiestnenie vybavenia a výrobných jednotiek obmedzené nedostatkom miesta alebo nadmernými nákladmi.
2–12
Cd + Tl
2–16
Použiteľné všeobecne na nové jednotky Použiteľnosť v prípade starých jednotiek môže byť obmedzená z dôvodu potreby dodatočného vybavenia spaľovacieho systému a/alebo systému riadenia.
BAT 27.
Použitie odstraňovania prachu suchou (napr. ESP alebo vrecovým filtrom) alebo mokrou (napr. mokrým ESP alebo práčkou plynu) cestou Ďalšie opisy sa nachádzajú v referenčnom dokumente o BAT pre výrobu železa a ocele.
In order to prevent or reduce mercury emissions to air from the combustion of solid biomass and/or peat, BAT is to use one or a combination of the techniques given below.
Priemyselné chladiace systémy (Industrial Cooling Systems, ICS)
80–96
Biologicky rozložiteľné organické zlúčeniny, amónium (NH4+)
BAT 28.
Použiteľné iba na tú časť zariadenia IGCC, ktorú tvorí plynová turbína.
Commission Implementing Decision (EU) 2017/1445
Vykonávacie rozhodnutie Komisie (EÚ) 2017/1445
of 8 August 2017
z 8. augusta 2017
on the group of products whose principal intended action, depending on proanthocyanidins (PAC) present in cranberry (Vaccinium macrocarpon), is to prevent or treat cystitis
o skupine výrobkov, ktorých hlavným určeným účinkom založeným na prítomnosti proantokyanidínov (PAC) v brusniciach (Vaccinium macrocarpon) je prevencia alebo liečba cystitídy
(notified under document C(2017) 5341)
[oznámené pod číslom C(2017) 5341]
Having regard to Council Directive 93/42/EEC of 14 June 1993 concerning medical devices [1], and in particular Article 13(1) thereof,
so zreteľom na smernicu Rady 93/42/EHS zo 14. júna 1993 o zdravotníckych pomôckach [1], a najmä na jej článok 13 ods. 1,
Having regard to the request submitted by France in accordance with Article 13(1)(d) of this Directive,
so zreteľom na žiadosť podanú Francúzskom v súlade s článkom 13 ods. 1 písm. d) uvedenej smernice,
France has requested the Commission in accordance with Article 13(1)(d) of Directive 93/42/EEC to take a decision that the group of products whose principal intended action, depending on proanthocyanidins (PAC) present in cranberry (Vaccinium macrocarpon) extract, is to prevent or treat cystitis, does not fall within the definition of medical devices set out in point (a) of Article 1(2) of Directive 93/42/EEC.
Francúzsko požiadalo v súlade s článkom 13 ods. 1 písm. d) smernice 93/42/EHS Komisiu, aby prijala rozhodnutie, že skupina výrobkov, ktorých hlavným určeným účinkom založeným na prítomnosti proantokyanidínov vo výťažku z brusníc (Vaccinium Macrocarpon) je prevencia alebo liečba cystitídy, nespadá do definície zdravotníckych pomôcok podľa článku 1 ods. 2 písm. a) smernice 93/42/EHS.
The definition of a medical device set out in Article 1(2)(a) of Directive 93/42/EEC provides among others that a device falls within that definition if it does not achieve its principal intended action by pharmacological, immunological or metabolic means.
V definícii zdravotníckej pomôcky uvedenej v článku 1 ods. 2 písm. a) smernice 93/42/EHS sa okrem iného stanovuje, že pomôcka spadá do uvedenej definície, pokiaľ nedosahuje svoj hlavný určený účinok farmakologickým, imunologickým alebo metabolickým spôsobom.
The European Medicines Agency (EMA) in its opinion of 22 July 2016 [2] concluded that the principal intended action of the group of products mentioned in recital (1) is achieved probably by pharmacological means as metabolites of PAC and other constituents of cranberry exhibit most probably a pharmacological activity and that a mechanical mode of action of PAC is highly unlikely.
Európska agentúra pre lieky (EMA) dospela vo svojom stanovisku z 22. júla 2016 [2] k záveru, že hlavný určený účinok skupiny výrobkov uvedených v bode 1 odôvodnenia sa pravdepodobne dosiahne farmakologickým spôsobom, keďže metabolity proantokyanidínov a ďalších zložiek obsiahnutých v brusniciach vykazujú s najväčšou pravdepodobnosťou farmakologické účinky, a že mechanický spôsob účinku proantokyanidínov je vysoko nepravdepodobný
The mechanical mode of action would indicate that the group of products in question fall within the definition of medical devices.
Mechanický spôsob účinku by znamenal, že dotknutá skupina výrobkov spadá do definície zdravotníckych pomôcok.
As such a mode is highly unlikely and a pharmacological mode of action is most probable, this indicates that the group of products in question should not fall within the definition of medical devices.
Vzhľadom na to, že takýto spôsob účinku je vysoko nepravdepodobný a farmakologický spôsob účinku je najviac pravdepodobný, znamená to, že dotknutá skupina výrobkov by nemala spadať do definície zdravotníckych pomôcok.
Results of a questionnaire circulated at the Medical Devices Expert Group in November 2014 showed that the majority of Member States, based on their scientific expertise, is of the view that this group of products should not fall within the definition of medical devices.
Z dotazníka, ktorý bol v novembri 2014 rozposlaný odbornej skupine pre zdravotnícke pomôcky, vyplynulo, že väčšina členských štátov je na základe odborných znalostí toho názoru, že uvedená skupina výrobkov by nemala spadať do definície zdravotníckych pomôcok.
The measures provided for in this Decision are in accordance with the opinion of the Committee established by Article 7(1) of Directive 93/42/EEC,
Opatrenia stanovené v tomto rozhodnutí sú v súlade so stanoviskom výboru zriadeného článkom 7 ods. 1 smernice 93/42/EHS.
The group of products whose principal intended action, depending on proanthocyanidins present in cranberry (Vaccinium macrocarpon) extract, is to prevent or treat cystitis, does not fall within the definition of medical devices set out in point (a) of Article 1(2) of Directive 93/42/EEC.
Skupina výrobkov, ktorých hlavným určeným účinkom založeným na prítomnosti proantokyanidínov vo výťažku z brusníc (Vaccinium macrocarpon) je prevencia alebo liečba cystitídy, nespadá do definície zdravotníckych pomôcok podľa článku 1 ods. 2 písm. a) smernice 93/42/EHS.
Done at Brussels, 8 August 2017.
V Bruseli 8. augusta 2017
OJ L 169, 12.7.1993, p. 1.
Ú. v. ES L 169, 12.7.1993, s. 1.
CHMP (Committee for Medicinal Products for Human Use) scientific opinion to DG Internal Market, Industry, Entrepreneurship and SMEs, Unit GROW D.4.
Vedecké stanovisko Výboru pre lieky na humánne použitie (CHMP) pre GR pre vnútorný trh, priemysel, podnikanie a malé a stredné podniky, oddelenie zdravotníckych technológií a kozmetiky, GROW D.4, o hlavnom spôsobe účinku proantokyanidínov zamýšľaných na prevenciu a liečbu infekcií močového ústrojenstva, EMA/427414/2016, http://ec.europa.eu/growth/tools-databases/newsroom/cf/itemdetail.cfm?item_id=8684&lang=en