Decree of the Ministry of Agriculture No. 141 / 1997 Coll.
Decree of the Ministry of Agriculture on technical requirements for the production, storage and processing of alcohol
Valid
Order
Effective from 01.07.1997
Zobrazeno prvních 200 z celkem 245 ustanovení tohoto předpisu.
Zobrazit celý předpis →
Pro stažení celého znění použijte tlačítko Stáhnout výše.
141
DECLARATION
Ministry of Agriculture
of 20 June 1997
on technical requirements for the production, storage and processing of alcohol
In agreement with the Ministry of Industry and Trade, the Ministry of Agriculture provides pursuant to § 21 paragraph 1 of Act No. 61 / 1997 Coll., on Lime and on Amendment and Addition of Act No. 455 / 1991 Coll., on Business Enterprise (Trade and Trade Act), as amended, and the Act of the Czech National Council No. 587 / 1992 Coll., on Consumer Taxes, as amended:
Technical requirements for the production facilities of distilleries and their layout
(to Section 5 of the Lime Act)
(1) This Decree was notified in accordance with Directive 98 / 34 / EC of the European Parliament and of the Council of 22 June 1998 laying down a procedure for the provision of information in the field of technical standards and regulations and rules and of rules on information society services, as amended by Directive 98 / 48 / EC.
(2) The production facilities of the distillery are instruments, pipes and spaces in which the alcohol and the alcohol vapours are not registered with a control alcohol meter (hereinafter referred to as the "measuring instrument '), as well as equipment for the collection of lutre waters and separated oils and waxes, the water resulting from the acquisition of alcohol in the manner laid down by law, after distillation separation of the alcohol.
(3) The distillery's production facilities are made of metal or other material resistant to alcohol, spirit vapours, operating temperatures and pressures.
(4) Only solders are used for soldering. Only materials resistant to change and temperature and pressure and alcohol and vapour are used for sealing.
(5) The pipes to which the alcohol and the spirit steam are conducted must not be damaged or repaired.
(6) Paintings of the distillery's manufacturing plant must not cover the composition of the material from which it is manufactured. If the pipes to which the alcohol and the spirit vapours, walls or ceilings are conducted pass through the pipe, the space for inspection shall be left around the pipe. This space shall be closed by covering the relevant technical standard (1).
(7) The coolant coupling line with the gauge shall have:
(a) progress,
(b) an internal diameter corresponding to the output of the distillation apparatus;
(c) tin cover on all joints (flanges, cocks, screws, etc.).
(8) The cover referred to in paragraph 7 (c) may be made of uncoated galvanized sheet or of other material conforming to the characteristics agreed by the controller (1a) and shall be adapted to the attached conclusions.
(9) Epruvets, sampling taps, air-conditioning devices, regulators of the amount of draining alcohol and devices to prevent vapour and vapour entry into the gauge shall be placed on the coolant coupling line with the gauge.
(10) If the reverse flow of alcohol to the boiling boiler of the distillation apparatus is returned, it shall:
(a) the supply welding pipe shall be fed into a special metal container fixed at the bottom of the distillery boiler so that the container remains filled with the match even after emptying the boiler and the supply line shall be completely immersed in the remaining steam,
(b) the discharge pipes shall be adjusted so as to leave the distillates at least 10 per cent of the volume of the boiler in the distillation boiler.
(11) In a chemical distillery where a circulatory (reflux) tank is used in the manufacture, the withdrawal of synthetic distillate from that tank shall be adjusted so that, when the alcohol is withdrawn from that tank, the withdrawal of the alcohol from that tank is carried out
(a) alcohol with a minimum content of higher alcohols and volatile substances specified for synthetic technical alcohol has been produced in the synthetic technical alcohol line;
(b) the alcohol has been discarded in the sewage tank by mixing with raw material for the manufacture of synthetic technical alcohol.
(12) In the distilleries where the seedlings and seedlings are taken to the lutre water collection facility, the mixture of levers and dregs shall be considered lutre water.
Technical requirements for continuous denaturing equipment
[Article 21 (1) (a) and (c) of the Lime Act]
(1) The supply line through which the denaturing agent is guided in continuous denaturing must be provided with a measuring device before the mouth into the lead alcohol pipe.
(2) The quantity of denaturant used for continuous denaturing of alcohol is measured by measuring instruments complying with the requirements of the Metrologii1b Act.
Technical requirements for alcohol storage facilities
(to Section 14 of the Lime Act)
(1) Equipment for the storage of alcohol is tanks, barrels, transport containers or packaging which meet the requirements laid down in the Metrologii1b Act (in which the measured alcohol is stored and transported.
(2) The alcohol storage facility is manufactured from a material resistant to alcohol exposure.
(3) The container shall be labelled with a volume marking.
(4) The tank shall be filled up to a maximum of 95 per cent of its volume.
(5) The fittings at the bottom of the tank are made of steel or brass. The container shall be equipped with a minimum diameter of 600 mm. The ventilation shall be connected to the highest part of the tank and adjusted so as not to contain alcohol or water.
(6) Tanks of more than 2 m shall be provided with a device enabling sampling to be carried out in each quarter of height or in the lid through an opening designed to trigger a sampling device allowing sampling from different layers.
Methods for determining the volume and concentration of alcohol and how to calculate the quantity of alcohol
[to Paragraph 21 (1) (b) of the Lime Act]
(1) For the determination of the volume and concentration of alcohol, except denatured alcohol, the measurement results shall be determined:
(a) the density determined by the pyknometric method;
(b) densities determined by the areometer meeting the conditions laid down in the Metrologii1b law for measurements at 20 degrees C;
(c) gas chromatography method;
(d) densities determined using an electronic frequency oscillator; or
(e) densities determined using hydrostatic scales.
In the case of alcohol denatured, the procedure laid down in paragraph 8 shall be followed.
(2) The volume concentration of alcohol in the chute is determined by the pyknometric method in the distillate from the water solution obtained by extraction of the chute with a petroleum ether for the addition of saturated sodium chloride solution or a gas chromatography method.
(3) The density of alcohol shall be calculated using the formula shown, including the coefficients in Annex 1, Part A.
(4) When determining the volume of alcohol in which the volume of alcohol is measured in the storage tanks of steel or in steel or britanium gauges provided for in the specific legislationm2), correction shall be made to the thermal volume expansion of these materials by multiplying the recorded volume of alcohol by the correction factor set out in Annex 1, Part B.
(5) When determining the volume concentration of alcohol by the pyknometric method, correction shall be made for the thermal volume expansion of pyknometers from different types of glass by multiplying the determined density by the correction factor set out in Annex 1, Part C.
(6) The calculation of the volume of ethanol shall be as set out in Annex 1, Part D.
(7) When using several measurement methods referred to in paragraph 1, the decisive result of the measurement carried out by the method of determination of density shall be pyknometric.
(8) For the determination of the volume concentration of denatured alcohol the measurement results are determined
(a) gas chromatography method; or
(b) liquid chromatography method.
(9) When using multiple measurement methods referred to in paragraph 8, the result of the measurement carried out by the gas chromatography method shall be decisive.
Type of denaturants and their minimum quantity and purpose of use of denatured alcohol
(to Section 10 of the Lime Act)
The types of denaturants, their minimum quantity and the purpose of using denatured alcohol are set out in Annex 2.
Breakdown of essential types of alcohol and their qualitative characteristics
(to Section 11 of the Lime Act)
(1) A more detailed breakdown of the basic types of alcohol and the qualitative characteristics of each type of alcohol are given in Annex 3.
(2) Specially denatured and generally denatured alcohol must meet the physical and chemical requirements laid down for the type of alcohol concerned and must comply with the applicable technical standards.
Methods for determining qualitative characteristics
(to Section 11 of the Lime Act)
(1) The methanol content is determined by the gas chromatography method.
(2) The content of higher alcohols is determined by the gas chromatography method and expressed as the sum of the determined levels of each higher alcohol.
(3) The content of aldehydes is determined colorimetric using a fuchsinsulphuric agent and evaluated as an acetaldehyde content or a gas chromatography method and expressed as the sum of the individual aldehydes.
(4) The fural content is determined by colorimetric method or by gas chromatography.
(5) The free acid content, the total content of which is evaluated as acetic acid content, is determined by titrating the sample of free carbon dioxide alcohol with a sodium hydroxide solution of 0,1 mol / l or a gas chromatography method, as appropriate.
(6) The content of nitrogen bases, the content of which is evaluated as the content of methylamine, is determined by titration of the sample with a solution of sulphuric acid of 0,005 mol / l to the Maa-Zuazaga indicator or bromocresol green or gas chromatography method.
(7) The area of the park is determined from a sample of 250 ml in the case of fermented refined fine undenatured alcohol or 100 ml in the case of other undenatured alcohol. After evaporation and drying of the sample at 103 ° C to 107 ° C and after cooling in the desiccator, the dried rest of the sample shall be weighed on the analytical scales.
(8) The ester content is determined by titrating a sample of alcohol with a 0,1 mol / l sodium hydroxide solution to the Simpson indicator and evaluated as an ethyl acetate or gas chromatography method and expressed as the sum of the individual esters.
(9) Diethyl ether and benzene content is determined by the gas chromatography method.
(10) The total content of higher alcohols and other volatile components for synthetic technical alcohol is determined by the gas chromatography method.
(11) The content of volatile denaturants in denatured alcohol is determined by the gas chromatography method.
(12) The distinction between yeast alcohol and synthetic alcohol is made by isotope methods.
(13) The content of Denatonium benzoate (Benzyldiethyl-N-2,6-xylyl carbamoyl methylammonium benzoate) is determined by a combination of gas chromatography with mass spectrometry or a combination of high performance liquid chromatography with mass spectrometry.
(14) The content of 2-methyl-2-propanol is determined by the gas chromatography method.
Lime loss standards
[to Paragraph 21 (1) (e) of the Lime Act]
The basis for calculating the different types of alcohol loss standards and their amounts are set out in Annex 4.
Traffic losses
[to Paragraph 2 (1) (k) of the Lime Act]
(1) Traffic losses are determined as the difference between the quantities of alcohol dispatched and the quantities accepted. Transport losses include losses that arise
(a) natural evaporation of alcohol during transport;
(b) as a result of the permissible differences in the measurement of the quantities of alcohol before and after dispatch.
(2) Transport losses shall not apply to quantities of alcohol contained in finished products made from alcohol.
(3) The drawing of the loss standard is assessed separately for each individual packaging. A quantity of alcohol in those packages for which no loss has been detected or for which a loss in excess of the standard loss has been found cannot be included in the basis for calculating the standard loss.
Manipulative losses
[to Paragraph 2 (1) (k) of the Lime Act]
Manipulative losses are losses of alcohol generated by the intake and issuing of alcohol and other technologically necessary handling of alcohol (overdrawing of alcohol by the producer and the alcohol processor). Such losses include losses incurred in the pumping of alcohol prior to the transport of alcohol in cases where the alcohol cannot be removed directly from the liquor store into the containers and the vats and the alcohol must first be pumped.
Loss of storage
[to Paragraph 2 (1) (k) of the Lime Act]
The losses of storage are losses of alcohol in the alcohol stores resulting from evaporation during storage.
Loss of bottling
[to Paragraph 2 (1) (k) of the Lime Act]
The losses of bottling shall be determined as the difference between the quantity of alcohol contained in the product intended for bottling and the quantity of alcohol contained in the finished product delivered to the processor's warehouse in the consumer package.
Loss on alcohol adjustments
[to Paragraph 2 (1) (k) of the Lime Act]
(1) The losses of refining shall be determined as the difference between the quantities of raw alcohol used for refining and the quantities of alcohol contained in refined alcohol and in drains, dopes and cloves.
(2) The loss of dehydration is determined as the difference between the quantity of alcohol used for dehydration and the quantity of alcohol contained in the produced anhydrous alcohol and other by-products of dehydration containing alcohol.
(3) The rectification losses shall be determined as the difference between the quantity of alcohol contained in the distillates intended for rectification and the quantity of alcohol contained in the rectified distillate and the stocks and imports.
(4) The losses of regeneration shall be determined as the difference between the quantity of alcohol contained in the substances from which the alcohol is to be recovered and the quantity of recovered alcohol.
Loss on alcohol processing
[to Paragraph 2 (1) (k) of the Lime Act]
The loss of alcohol during the processing of alcohol shall be determined as the difference between the quantity of alcohol used for production and the quantity of alcohol contained in the semi-finished product or in the finished product.
Transitional provision
The calculation of the alcohol loss standards is carried out according to existing rules
(a) in distilleries of industrial, special distilleries carrying out the refining of alcohol or the refining of distillates, and in the Liquefaction Board until 30 September 1997;
(b) in agricultural and fruit distilleries until the date of completion of seasonal production and in continuous production until 30 September 1997;
(c) distilleries and special distilleries other than those referred to in (a) and (b) and in the case of producers of spirit drinks and other processors of alcohol, including vinegar, until 31 December 1997;
(d) distilleries which are also producers of spirit drinks until the date of the end of seasonal production of alcohol and in continuous production of alcohol until 30 September 1997.
Efficacy
This Decree shall take effect on 1 July 1997.
Minister:
Ing. Lux v. r.
Příloha č. 1
Annex No 1 to Decree No 141 / 1997 Coll.
MODEL FOR CALCULATION OF THE STRENGTH
IUPAC Name
= 1n = 1m1 Ci, k pk t-200 Ci.
n = 5
m1 = 11
m2 = 10
m3 = 9
m4 = 4
m5 = 2
Value of coefficients:
| k | Ak kg/m3 | Bk |
|---|---|---|
| 1 | 9,982 012 300 • 102 | -2,061 851 3 • 10-1 kg/(m3 • °C) |
| 2 | - 1,929 769 495 • 102 | - 5,268 254 2 • 10-3 kg/(m3 • °C2) |
| 3 | 3,891 238 958 • 102 | 3,613 001 3 • 10-5 kg/(m3 • °C3) |
| 4 | - 1,668 103 923 • 103 | - 3,895 770 2 • 10-7 kg/(m3 • °C4) |
| 5 | 1,352 215 441 • 104 | 7,169 354 0 • 10-9 kg/(m3 • °C5) |
| 6 | - 8,829 278 388 • 104 | -9,973 923 1 • 10-11 kg/(m3 • °C6) |
| 7 | 3,062 874 042 • 105 | |
| 8 | - 6,138 381 234 • 105 | |
| 9 | 7,470 172 998 • 105 | |
| 10 | - 5,478 461 354 • 105 | |
| 11 | 2,234 460 334 • 105 | |
| 12 | - 3,903 285 426 • 104 |
| C1,k kg/(m3 • °C) | C2,k kg/(m3 • °C2) | |
|---|---|---|
| 1 | 1,693 443 461 530 087 • 10-1 | -1,193 013 005 057 010 • 10-2 |
| 2 | -1,046 914 743 455 169 • 101 | 2,517 399 633 803 461 • 10-1 |
| 3 | 7,196 353 469 546 523 • 101 | -2,170 575 700 536 993 |
| 4 | -7,047 478 054 272 792 • 102 | 1,353 034 988 843 029 • 101 |
| 5 | 3,924 090 430 035 045 • 103 | -5,029 988 758 547 014 • 101 |
| 6 | -1,210 164 659 068 747 • 104 | 1,096 355 666 577 570 • 102 |
| 7 | 2,248 646 550 400 788 • 104 | -1,422 753 946 421 155 • 102 |
| 8 | -2,605 562 982 188 164 • 104 | 1,080 435 942 856 230 • 102 |
| 9 | 1,852 373 922 069 467 • 104 | -4,414 153 236 817 392 • 101 |
| 10 | -7,420 201 433 430 137 • 103 | 7,442 971 530 188 783 |
| 11 | 1,285 617 841 998 974 • 103 |
| k | C3,k kg/(m3 • °C3) | C4,k kg/(m3 • °C4) | C5,k kg/(m3 • °C5) |
|---|---|---|---|
| 1 | -6,802 995 733 503 803 • 10-4 | 4,075 376 675 622 027 • 10-6 | -2,788 074 354 782 409 • 10-8 |
| 2 | 1,876 837 790 289 664 • 10-2 | -8,763 058 573 471110 • 10-6 | 1,345 612 883 493 354 • 10-8 |
| 3 | -2,002 561 813 734 156 • 10-1 | 6,515 031 360 099 368 • 10-6 | |
| 4 | 1,022 992 966 719 220 | -1,515 784 836 987 210 • 10-6 | |
| 5 | -2,895 696 483 903 638 | ||
| 6 | 4,810 060 584 300 675 | ||
| 7 | -4,672 147 440 794 683 | ||
| 8 | 2,458 043105 903 461 | ||
| 9 | -5,411 227 621 436 812 • 10-1 |
Note:
1. This formula applies to measurements made at temperatures ranging from - 20 ° C to + 40 ° C.
2. Values derived from this formula are calculated in the Official alcoholic tables (part 1 - 3), issued by the Ministry of Agriculture of the Czech Republic, Prague 1995.
Table of correction factors (Fb) for the correction to the thermal volume expansion of the material at t (in ° C-1)
Material: Steel
Temperature coefficient of volume expansion (β) = 36.10- 6 ° C-1
| t | Fb |
|---|---|
| -20 | 0,99856 |
| -19 | 0,99860 |
| -18 | 0,99863 |
| -17 | 0,99867 |
| -16 | 0,99870 |
| -15 | 0,99874 |
| -14 | 0,99878 |
| -13 | 0,99881 |
| -12 | 0,99885 |
| -11 | 0,99888 |
| -10 | 0,99892 |
| -9 | 0,99896 |
| -8 | 0,99899 |
| -7 | 0,99903 |
| -6 | 0,99906 |
| -5 | 0,99910 |
| -4 | 0,99914 |
| -3 | 0,99917 |
| -2 | 0,99921 |
| -1 | 0,99924 |
| 0 | 0,99928 |
| 1 | 0,99932 |
| 2 | 0,99935 |
| 3 | 0,99939 |
| 4 | 0,99942 |
| 5 | 0,99946 |
| 6 | 0,99950 |
| 7 | 0,99953 |
| 8 | 0,99957 |
| 9 | 0,99960 |
| 10 | 0,99964 |
| 10 | 0,99964 |
| 11 | 0,99968 |
| 12 | 0,99971 |
| 13 | 0,99975 |
| 14 | 0,99978 |
| 15 | 0,99982 |
| 16 | 0,99986 |
| 17 | 0,99989 |
| 18 | 0,99993 |
| 19 | 0,99996 |
| 20 | 1,00000 |
| 21 | 1,00004 |
| 22 | 1,00007 |
| 23 | 1,00011 |
| 24 | 1,00014 |
| 25 | 1,00018 |
| 26 | 1,00022 |
| 27 | 1,00025 |
| 28 | 1,00029 |
| 29 | 1,00032 |
| 30 | 1,00036 |
| 31 | 1,00040 |
| 32 | 1,00043 |
| 33 | 1,00047 |
| 34 | 1,00050 |
| 35 | 1,00054 |
| 36 | 1,00058 |
| 37 | 1,00061 |
| 38 | 1,00065 |
| 39 | 1,00068 |
| 40 | 1,00072 |
Material: Britanium
Temperature coefficient of volume expansion (β) = 61.10- 6 ° C-1
| t | Fb |
|---|---|
| 0 | 0,99878 |
| 1 | 0,99884 |
| 2 | 0,99890 |
| 3 | 0,99896 |
| 4 | 0,99902 |
| 5 | 0,99909 |
| 6 | 0,99915 |
| 7 | 0,99921 |
| 8 | 0,99927 |
| 9 | 0,99933 |
| 10 | 0,99939 |
| 11 | 0,99945 |
| 12 | 0,99951 |
| 13 | 0,99957 |
| 14 | 0,99963 |
| 15 | 0,99970 |
| 16 | 0,99976 |
| 17 | 0,99982 |
| 18 | 0,99988 |
| 19 | 0,99994 |
| 20 | 1,00000 |
| 20 | 1,00000 |
| 21 | 1,00006 |
| 22 | 1,00012 |
| 23 | 1,00018 |
| 24 | 1,00024 |
| 25 | 1,00031 |
| 26 | 1,00037 |
| 27 | 1,00043 |
| 28 | 1,00049 |
| 29 | 1,00055 |
| 30 | 1,00061 |
| 31 | 1,00067 |
| 32 | 1,00073 |
| 33 | 1,00079 |
| 34 | 1,00085 |
| 35 | 1,00092 |
| 36 | 1,00098 |
| 37 | 1,00104 |
| 38 | 1,00110 |
| 39 | 1,00116 |
| 40 | 1,00122 |
Table of correction factors (Fb) for the correction to the thermal volume expansion of pyknometers from different types of glass at t (in ° C-1)
Temperature coefficient of volume expansion (β) column:
(a) = 5.10- 6 ° C-1
(b) = 10.10-6 ° C-1
(c) = 15.10- 6 ° C-1
(d) = 20.10-6 ° C-1
(e) = 25.10-6 ° C-1
f) = 30.10- 6 ° C-1
(g) glass of normal quartz = 1,6.10- 6 ° C-1
(h) glass normal Simax = 8,8.10- 6 ° C-1
(i) glass normal Sial = 13,0.10- 6 ° C-1
(j) glass normal Neutral = 17,0.10-6 ° C-1
k) Glass normal KS = 24,0.10 -6 ° C-1
(l) glass normal Unihost = 27,0.10-6 ° C-1
t / column
| a) | b) | c) | d) | e) | f) | g) | h) | i) | j) | k) | l) | |
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 15 | 1,000025 | 1,000050 | 1,000075 | 1,000100 | 1,000125 | 1,000150 | 1,000008 | 1,000044 | 1,000065 | 1,000087 | 1,000122 | 1,000135 |
| 16 | 1,000020 | 1,000040 | 1,000060 | 1,000080 | 1,000100 | 1,000120 | 1,000006 | 1,000035 | 1,000052 | 1,000070 | 1,000097 | 1,000108 |
| 17 | 1,000015 | 1,000030 | 1,000045 | 1,000060 | 1,000075 | 1,000090 | 1,000005 | 1,000026 | 1,000039 | 1,000052 | 1,000073 | 1,000081 |
| 18 | 1,000010 | 1,000020 | 1,000030 | 1,000040 | 1,000050 | 1,000060 | 1,000003 | 1,000018 | 1,000026 | 1,000035 | 1,000049 | 1,000054 |
| 19 | 1,000005 | 1,000010 | 1,000015 | 1,000020 | 1,000025 | 1,000030 | 1,000002 | 1,000009 | 1,000013 | 1,000017 | 1,000024 | 1,000027 |
| 20 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 | 1,000000 |
| 21 | 0,999995 | 0,999990 | 0,999985 | 0,999980 | 0,999975 | 0,999970 | 0,999998 | 0,999991 | 0,999987 | 0,999983 | 0,999976 | 0,999973 |
| 22 | 0,999990 | 0,999980 | 0,999970 | 0,999960 | 0,999950 | 0,999940 | 0,999997 | 0,999982 | 0,999974 | 0,999965 | 0,999951 | 0,999946 |
| 23 | 0,999985 | 0,999970 | 0,999955 | 0,999940 | 0,999925 | 0,999910 | 0,999995 | 0,999974 | 0,999961 | 0,999948 | 0,999927 | 0,999919 |
| 24 | 0,999980 | 0,999960 | 0,999940 | 0,999950 | 0,999900 | 0,999880 | 0,999994 | 0,999965 | 0,999948 | 0,999930 | 0,999903 | 0,999892 |
| 25 | 0,999975 | 0,999950 | 0,999924 | 0,999900 | 0,999875 | 0,999850 | 0,999992 | 0,999956 | 0,999935 | 0,999913 | 0,999879 | 0,999865 |
Method of calculating the volume of ethanol
(a) the calculation of the volume of ethanol VE (unit: m3 or L = dm3) when weighing ethanol solution and water shall be carried out according to the formula:
VE = Z. km
where VE is the volume of ethanol at 20 ° C in litres
Z is the apparent mass of ethanol solution and water determined by weighing in air (unit: kg)
km is the conversion coefficient (unit: dm3 / kg = L / kg) calculated according to the formula:
km = σE iS 10ρ20 iS 1 + ρa 1ρ20-1ρZ
where σE is the volume concentration of ethanol in ethanol and water solution (unit:% = 0,01)
ρ20 is the density of the solution at 20 ° C (unit: kg / m3)
ρa is the density of air (unit: kg / m3, adopted value: 1,2 kg / m3)
ρZ is the weight density (unit: kg / m3, accepted value: 8000 kg / m3)
(b) The calculation of the volume of ethanol VE (unit: m3 or L = dm3) when measuring the volume of ethanol solution and water by means of a volume gauge of between - 20 ° C and + 40 ° C shall be carried out according to the formula:
Sign in for notes, favorites and notifications
Regulation Information
| Citation | Decree of the Ministry of Agriculture No. 141 / 1997 Coll., on technical requirements for the production, storage and processing of alcohol |
|---|---|
| Regulation Type | Order |
| Author | - |
| Collection | Code of Laws |
| Date of Promulgation | 30.06.1997 |
|---|---|
| Effective from | 01.07.1997 |
| Effective until | - |
| Status | Valid |
The regulation text is for informational purposes only.
Comments 0