WAC 16-659-010

WAC 16-659-010. Liquefied petroleum gas

Last amended: 1998Year: 2026Length: 2,594 wordsOfficial source
(1) Liquefied petroleum gas shall be sold or exposed for sale at retail only by avoirdupois weight, specified in pounds; liquid measure, specified in gallons; or vapor, specified in cubic feet. (2) When sold by weight or by liquid measure or in units of cubic feet, it shall be dispensed and sold only by the use of such devices that conform to the requirements set forth in National Institute of Standards and Technology Handbook 44 , edition specified in chapter 16-662 WAC. (3) Liquefied petroleum gas sold or delivered to a consumer by liquid measure shall be corrected to a temperature of 60 F with an automatic correction device, or the quantity delivered shall be corrected to a temperature of 60 F in accordance with the volume correction factor table for liquefied petroleum gases set forth in subsection (6) of this chapter. When the delivery is made through a meter automatically corrected for temperature, the retail sales ticket shall show the meter adjusted gallons delivered and state that the temperature correction was made automatically. When the delivery is made through a meter not corrected automatically, the retail sales ticket shall show the metered gallons delivered and the temperature of the liquid at the time of delivery, the volume correction factor and the corrected gallonage: Provided, That this section shall be applicable to new equipment, equipment that has changed ownership or equipment used in the state of Washington for the first time after the effective date of this section. This subsection shall be applicable to all other equipment and with respect to the manual issuances of sales tickets as of January 1, 1969. This subsection shall not apply to unit sales or deliveries made direct to fuel tanks on trucks and automobiles operated on highways, or to containers of less than 200 pound water capacity. (4) If a device is equipped with an automatic temperature compensator, this shall be connected, operable, and used at all times. Such automatic temperature compensator may not be removed, nor may a compensated device be replaced with an uncompensated device, without the written approval of the weights and measures authority having jurisdiction over the device. Nothing in this subsection shall prohibit the removal of a meter or temperature compensator for repair providing notice of such removal for repair shall be given the weights and measures office in Olympia within three working days. (5)(a) Containers, including I.C.C. cylinders, with water capacity less than 200 pounds, shall be charged and sold by weight or by metered measure, except containers excluded by law or regulation. The tare weight of the container and the net weight of the contents shall be plainly and conspicuously marked on the outside of the container or on a label firmly attached thereto. This subsection shall not be construed to require the net weight to be labeled on a container that is being filled at the time of sale. Tare weight shall not be construed to include the valve protecting cap which shall be removed when weighing. When liquefied petroleum gas is sold by refilling of a container the vendor shall give the purchaser full credit for the unused liquid remaining in the container being refilled. When liquefied petroleum gas is sold by an exchange of containers the vendor shall specify conspicuously on a label firmly attached to the container the following: Tare weight of the container, the net weight of the contents and the name and address of the facility where the tank was filled. The address shall include the street address, city, state and zip code. Tare weight shall not be construed to include the valve protecting cap. The cap shall be removed when weighing. (b) A delivery ticket shall be issued at the time of filling and shall set forth the exact amount of liquefied petroleum gas dispensed in terms of weight or if converted to gallons the weight factor used in such conversion. Any service charge shall be shown separately on the delivery ticket but may be included in the total price. (c) When sold by weight, the tare weight, any unused portion and/or the net weight shall be determined only on devices that are adequately protected from wind and weather conditions that will assure normal accuracy. (6) Volume correction factor table. Specific Gravity at 60 F/60 F [CODIFICATION NOTE: THE GRAPHIC PRESENTATION OF THESE TABLES HAS BEEN VARIED SLIGHTLY IN ORDER THAT THEY WOULD FALL WITHIN THE PRINTING SPECIFICATIONS FOR THE WASHINGTON ADMINISTRATIVE CODE. THE FOLLOWING TABLE WAS TOO WIDE TO BE ACCOMMODATED IN THE WIDTH OF THE WAC COLUMN. THE TABLE AS CODIFIED HAS BEEN DIVIDED INTO TWO TABLES COVERING THE "SPECIFIC GRAVITY AT 60 F/60 F." PART ONE IS FOR 0.500, 0.5079, 0.510, 0.520, 0.530, AND 0.540. PART TWO IS FOR 0.550, 0.560, 0.5631, 0.570, 0.580, AND 0.5844.] [PART 1—0.500, 0.5079, etc.] Degrees Fahr 0.500 Propane 0.5079 0.510 0.520 0.530 0.540 VOLUME CORRECTION FACTORS -15 1.112 1.109 1.107 1.102 1.097 1.093 -10 1.105 1.102 1.100 1.095 1.091 1.087 - 5 1.098 1.094 1.094 1.078 1.085 1.081 0 1.092 1.088 1.088 1.084 1.080 1.076 2 1.089 1.086 1.085 1.081 1.077 1.074 4 1.086 1.083 1.082 1.079 1.075 1.071 6 1.084 1.080 1.080 1.076 1.072 1.069 8 1.081 1.078 1.077 1.074 1.070 1.066 10 1.078 1.075 1.074 1.071 1.067 1.064 12 1.075 1.072 1.071 1.068 1.064 1.061 14 1.072 1.070 1.069 1.066 1.062 1.059 16 1.070 1.067 1.066 1.063 1.060 1.056 18 1.067 1.065 1.064 1.061 1.057 1.054 20 1.064 1.062 1.061 1.058 1.054 1.051 22 1.061 1.059 1.058 1.055 1.052 1.049 24 1.058 1.056 1.055 1.052 1.049 1.046 26 1.055 1.053 1.052 1.049 1.047 1.044 28 1.052 1.050 1.049 1.047 1.044 1.041 30 1.049 1.047 1.046 1.044 1.041 1.039 32 1.046 1.044 1.043 1.041 1.038 1.036 34 1.043 1.041 1.040 1.038 1.036 1.034 36 1.039 1.038 1.037 1.035 1.033 1.031 38 1.036 1.035 1.034 1.032 1.031 1.029 40 1.033 1.032 1.031 1.029 1.028 1.026 42 1.030 1.029 1.028 1.026 1.025 1.023 44 1.027 1.026 1.025 1.023 1.022 1.021 46 1.023 1.022 1.022 1.021 1.020 1.018 48 1.020 1.019 1.019 1.018 1.017 1.016 50 1.017 1.016 1.016 1.015 1.014 1.013 52 1.014 1.013 1.012 1.012 1.011 1.010 54 1.010 1.010 1.009 1.009 1.008 1.007 56 1.007 1.007 1.006 1.006 1.005 1.005 58 1.003 1.003 1.003 1.003 1.003 1.002 60 1.000 1.000 1.000 1.000 1.000 1.000 62 0.997 0.997 0.997 0.997 0.997 0.997 64 0.993 0.993 0.994 0.994 0.994 0.994 66 0.991 0.990 0.990 0.990 0.991 0.992 68 0.986 0.986 0.987 0.987 0.988 0.989 70 0.983 0.983 0.984 0.984 0.985 0.986 72 0.979 0.980 0.981 0.981 0.982 0.983 74 0.976 0.975 0.977 0.978 0.980 0.980 76 0.972 0.973 0.974 0.975 0.977 0.978 78 0.969 0.970 0.970 0.972 0.974 0.975 80 0.965 0.966 0.967 0.969 0.971 0.972 82 0.961 0.963 0.963 0.966 0.968 0.969 84 0.957 0.959 0.960 0.962 0.965 0.966 86 0.954 0.956 0.956 0.959 0.961 0.964 88 0.950 0.952 0.953 0.955 0.958 0.961 90 0.946 0.949 0.949 0.952 0.955 0.958 92 0.942 0.945 0.946 0.949 0.952 0.955 94 0.938 0.941 0.942 0.946 0.949 0.952 96 0.935 0.938 0.939 0.942 0.946 0.949 98 0.931 0.934 0.935 0.939 0.943 0.946 100 0.927 0.930 0.932 0.936 0.940 0.943 105 0.918 0.920 0.923 0.927 0.932 0.935 110 0.907 0.911 0.913 0.918 0.923 0.927 115 0.897 0.901 0.904 0.910 0.915 0.920 120 0.887 0.892 0.894 0.900 0.907 0.912 Degrees Fahr 0.500 Propane 0.5079 0.510 0.520 0.530 0.540 VOLUME CORRECTION FACTORS -15 1.112 1.109 1.107 1.102 1.097 1.093 -10 1.105 1.102 1.100 1.095 1.091 1.087 - 5 1.098 1.094 1.094 1.078 1.085 1.081 0 1.092 1.088 1.088 1.084 1.080 1.076 2 1.089 1.086 1.085 1.081 1.077 1.074 4 1.086 1.083 1.082 1.079 1.075 1.071 6 1.084 1.080 1.080 1.076 1.072 1.069 8 1.081 1.078 1.077 1.074 1.070 1.066 10 1.078 1.075 1.074 1.071 1.067 1.064 12 1.075 1.072 1.071 1.068 1.064 1.061 14 1.072 1.070 1.069 1.066 1.062 1.059 16 1.070 1.067 1.066 1.063 1.060 1.056 18 1.067 1.065 1.064 1.061 1.057 1.054 20 1.064 1.062 1.061 1.058 1.054 1.051 22 1.061 1.059 1.058 1.055 1.052 1.049 24 1.058 1.056 1.055 1.052 1.049 1.046 26 1.055 1.053 1.052 1.049 1.047 1.044 28 1.052 1.050 1.049 1.047 1.044 1.041 30 1.049 1.047 1.046 1.044 1.041 1.039 32 1.046 1.044 1.043 1.041 1.038 1.036 34 1.043 1.041 1.040 1.038 1.036 1.034 36 1.039 1.038 1.037 1.035 1.033 1.031 38 1.036 1.035 1.034 1.032 1.031 1.029 40 1.033 1.032 1.031 1.029 1.028 1.026 42 1.030 1.029 1.028 1.026 1.025 1.023 44 1.027 1.026 1.025 1.023 1.022 1.021 46 1.023 1.022 1.022 1.021 1.020 1.018 48 1.020 1.019 1.019 1.018 1.017 1.016 50 1.017 1.016 1.016 1.015 1.014 1.013 52 1.014 1.013 1.012 1.012 1.011 1.010 54 1.010 1.010 1.009 1.009 1.008 1.007 56 1.007 1.007 1.006 1.006 1.005 1.005 58 1.003 1.003 1.003 1.003 1.003 1.002 60 1.000 1.000 1.000 1.000 1.000 1.000 62 0.997 0.997 0.997 0.997 0.997 0.997 64 0.993 0.993 0.994 0.994 0.994 0.994 66 0.991 0.990 0.990 0.990 0.991 0.992 68 0.986 0.986 0.987 0.987 0.988 0.989 70 0.983 0.983 0.984 0.984 0.985 0.986 72 0.979 0.980 0.981 0.981 0.982 0.983 74 0.976 0.975 0.977 0.978 0.980 0.980 76 0.972 0.973 0.974 0.975 0.977 0.978 78 0.969 0.970 0.970 0.972 0.974 0.975 80 0.965 0.966 0.967 0.969 0.971 0.972 82 0.961 0.963 0.963 0.966 0.968 0.969 84 0.957 0.959 0.960 0.962 0.965 0.966 86 0.954 0.956 0.956 0.959 0.961 0.964 88 0.950 0.952 0.953 0.955 0.958 0.961 90 0.946 0.949 0.949 0.952 0.955 0.958 92 0.942 0.945 0.946 0.949 0.952 0.955 94 0.938 0.941 0.942 0.946 0.949 0.952 96 0.935 0.938 0.939 0.942 0.946 0.949 98 0.931 0.934 0.935 0.939 0.943 0.946 100 0.927 0.930 0.932 0.936 0.940 0.943 105 0.918 0.920 0.923 0.927 0.932 0.935 110 0.907 0.911 0.913 0.918 0.923 0.927 115 0.897 0.901 0.904 0.910 0.915 0.920 120 0.887 0.892 0.894 0.900 0.907 0.912 To convert from measured volume at another temperature to net volume at 60°F: Measure the volume and temperature. Determine the gravity at 60°F. Refer to the column corresponding to this gravity and read the volume conversion factor opposite the observed temperature. Multiply the observed volume by this factor to obtain the volume at 60°F. [PART 2—0.550, 0.560, etc.] Degrees Fahr 0.550 iso-Butane 0.560 0.5631 0.570 0.580 N-Butane 0.5844 VOLUME CORRECTION FACTORS -15 1.089 1.084 1.083 1.080 1.077 1.075 -10 1.083 1.079 1.078 1.075 1.072 1.071 - 5 1.077 1.074 1.073 1.070 1.067 1.060 0 1.073 1.069 1.068 1.066 1.063 1.062 2 1.070 1.067 1.066 1.064 1.061 1.060 4 1.068 1.065 1.064 1.062 1.059 1.058 6 1.065 1.062 1.061 1.059 1.057 1.055 8 1.063 1.060 1.059 1.057 1.055 1.059 10 1.061 1.058 1.057 1.055 1.053 1.051 12 1.059 1.056 1.055 1.053 1.051 1.049 14 1.056 1.053 1.053 1.051 1.049 1.047 16 1.054 1.051 1.050 1.048 1.046 1.045 18 1.051 1.049 1.048 1.046 1.044 1.043 20 1.049 1.046 1.046 1.044 1.042 1.041 22 1.046 1.044 1.044 1.042 1.040 1.040 24 1.044 1.042 1.042 1.040 1.038 1.037 26 1.042 1.039 1.039 1.037 1.036 1.036 28 1.039 1.037 1.037 1.035 1.034 1.034 30 1.037 1.035 1.035 1.033 1.032 1.032 32 1.035 1.033 1.033 1.031 1.030 1.030 34 1.032 1.031 1.030 1.029 1.028 1.028 36 1.030 1.028 1.028 1.027 1.025 1.025 38 1.027 1.026 1.025 1.025 1.023 1.023 40 1.025 1.024 1.023 1.023 1.021 1.021 42 1.023 1.022 1.021 1.021 1.019 1.019 44 1.020 1.019 1.019 1.018 1.017 1.017 46 1.018 1.017 1.016 1.016 1.015 1.015 48 1.015 1.014 1.014 1.013 1.013 1.016 50 1.013 1.012 1.012 1.011 1.011 1.011 52 1.101 1.009 1.009 1.009 1.009 1.009 54 1.007 1.007 1.007 1.007 1.006 1.006 56 1.005 1.005 1.005 1.005 1.004 1.004 58 1.002 1.002 1.002 1.002 1.002 1.002 60 1.000 1.000 1.000 1.000 1.000 1.000 62 0.997 0.998 0.998 0.998 0.998 0.998 64 0.995 0.995 0.995 0.995 0.996 0.996 66 0.992 0.993 0.993 0.993 0.993 0.993 68 0.990 0.990 0.990 0.990 0.991 0.991 70 0.987 0.988 0.988 0.988 0.989 0.989 72 0.984 0.985 0.986 0.986 0.987 0.987 74 0.982 0.983 0.983 0.984 0.985 0.985 76 0.979 0.980 0.981 0.981 0.982 0.982 78 0.977 0.978 0.978 0.979 0.980 0.980 80 0.974 0.975 0.976 0.977 0.978 0.978 82 0.971 0.972 0.973 0.974 0.976 0.976 84 0.968 0.970 0.971 0.972 0.974 0.974 86 0.966 0.967 0.968 0.969 0.972 0.972 88 0.963 0.965 0.966 0.967 0.969 0.969 90 0.960 0.962 0.963 0.964 0.967 0.967 92 0.957 0.959 0.960 0.962 0.964 0.965 94 0.954 0.957 0.958 0.959 0.962 0.962 96 0.952 0.954 0.955 0.957 0.959 0.960 98 0.949 0.952 0.953 0.954 0.957 0.957 100 0.946 0.949 0.950 0.952 0.954 0.955 105 0.939 0.943 0.943 0.946 0.949 0.949 110 0.932 0.936 0.937 0.939 0.943 0.944 115 0.925 0.930 0.930 0.933 0.937 0.938 120 0.918 0.923 0.924 0.927 0.931 0.932 Degrees Fahr 0.550 iso-Butane 0.560 0.5631 0.570 0.580 N-Butane 0.5844 VOLUME CORRECTION FACTORS -15 1.089 1.084 1.083 1.080 1.077 1.075 -10 1.083 1.079 1.078 1.075 1.072 1.071 - 5 1.077 1.074 1.073 1.070 1.067 1.060 0 1.073 1.069 1.068 1.066 1.063 1.062 2 1.070 1.067 1.066 1.064 1.061 1.060 4 1.068 1.065 1.064 1.062 1.059 1.058 6 1.065 1.062 1.061 1.059 1.057 1.055 8 1.063 1.060 1.059 1.057 1.055 1.059 10 1.061 1.058 1.057 1.055 1.053 1.051 12 1.059 1.056 1.055 1.053 1.051 1.049 14 1.056 1.053 1.053 1.051 1.049 1.047 16 1.054 1.051 1.050 1.048 1.046 1.045 18 1.051 1.049 1.048 1.046 1.044 1.043 20 1.049 1.046 1.046 1.044 1.042 1.041 22 1.046 1.044 1.044 1.042 1.040 1.040 24 1.044 1.042 1.042 1.040 1.038 1.037 26 1.042 1.039 1.039 1.037 1.036 1.036 28 1.039 1.037 1.037 1.035 1.034 1.034 30 1.037 1.035 1.035 1.033 1.032 1.032 32 1.035 1.033 1.033 1.031 1.030 1.030 34 1.032 1.031 1.030 1.029 1.028 1.028 36 1.030 1.028 1.028 1.027 1.025 1.025 38 1.027 1.026 1.025 1.025 1.023 1.023 40 1.025 1.024 1.023 1.023 1.021 1.021 42 1.023 1.022 1.021 1.021 1.019 1.019 44 1.020 1.019 1.019 1.018 1.017 1.017 46 1.018 1.017 1.016 1.016 1.015 1.015 48 1.015 1.014 1.014 1.013 1.013 1.016 50 1.013 1.012 1.012 1.011 1.011 1.011 52 1.101 1.009 1.009 1.009 1.009 1.009 54 1.007 1.007 1.007 1.007 1.006 1.006 56 1.005 1.005 1.005 1.005 1.004 1.004 58 1.002 1.002 1.002 1.002 1.002 1.002 60 1.000 1.000 1.000 1.000 1.000 1.000 62 0.997 0.998 0.998 0.998 0.998 0.998 64 0.995 0.995 0.995 0.995 0.996 0.996 66 0.992 0.993 0.993 0.993 0.993 0.993 68 0.990 0.990 0.990 0.990 0.991 0.991 70 0.987 0.988 0.988 0.988 0.989 0.989 72 0.984 0.985 0.986 0.986 0.987 0.987 74 0.982 0.983 0.983 0.984 0.985 0.985 76 0.979 0.980 0.981 0.981 0.982 0.982 78 0.977 0.978 0.978 0.979 0.980 0.980 80 0.974 0.975 0.976 0.977 0.978 0.978 82 0.971 0.972 0.973 0.974 0.976 0.976 84 0.968 0.970 0.971 0.972 0.974 0.974 86 0.966 0.967 0.968 0.969 0.972 0.972 88 0.963 0.965 0.966 0.967 0.969 0.969 90 0.960 0.962 0.963 0.964 0.967 0.967 92 0.957 0.959 0.960 0.962 0.964 0.965 94 0.954 0.957 0.958 0.959 0.962 0.962 96 0.952 0.954 0.955 0.957 0.959 0.960 98 0.949 0.952 0.953 0.954 0.957 0.957 100 0.946 0.949 0.950 0.952 0.954 0.955 105 0.939 0.943 0.943 0.946 0.949 0.949 110 0.932 0.936 0.937 0.939 0.943 0.944 115 0.925 0.930 0.930 0.933 0.937 0.938 120 0.918 0.923 0.924 0.927 0.931 0.932 To convert from measured volume at another temperature to net volume at 60°F: Measure the volume and temperature. Determine the gravity at 60°F. Refer to the column corresponding to this gravity and read the volume conversion factor opposite the observed temperature. Multiply the observed volume by this factor to obtain the volume at 60°F.
WAC 16-659-010: WAC 16-659-010. Liquefied petroleum gas | Justis AI