Apparatus and method for measuring height of solid bed in high-temperature and high-pressure fluidized bed system

A solid bed height measuring apparatus in a high-temperature and high-pressure fluidized bed system comprising:

• a lower pressure probe which is mounted at an upper side as high as a first height from a gas distributor of a fluidized bed reactor to measure pressure of the mounted location;
• a middle pressure probe which is mounted at an upper side as high as a second height from the lower probe to measure pressure of the mounted location;
• an upper pressure probe which is mounted at the top of the fluidized bed reactor to measure the inside pressure of the fluidized bed reactor;
• the lower pressure probe and the middle pressure probe being mounted to exist inside the solid bed under all operation conditions, and the upper pressure probe being mounted at the upper side of the fluidized bed reactor, where the solid bed cannot reach, under all operation conditions;
• a differential pressure type pressure converter for measuring differential pressure values based on a first pressure value measured by the lower pressure probe, a second pressure value measured by the middle pressure probe and a third pressure value measured by the upper pressure probe, the different pressure type converter measuring a first differential pressure value (ΔP1) which is a differential pressure between the first pressure value and the second pressure value, and a second differential pressure value (ΔP2) which is a differential pressure between the first pressure value and the third pressure value;
• and
• a height arithmetic part for calculating a height of the solid bed inside the fluidized bed reactor based on the first differential pressure value (ΔP1) and the second differential pressure value (ΔP2);
• wherein the height arithmetic part calculates:
• a height arithmetic constant value (a)
• a
• =
• g
• c
• (
• 1
• -
• ɛ
• mf
• )
• ⁢
• (
• ρ
• s
• -
• ρ
• g
• )
• ⁢
• g
• (wherein εmf is a voidage of the solid bed under the minimum fluidization condition, ρs is density of the solid, μg is density of the gas, gc is a gravitational acceleration constant, and g is acceleration of gravity) from the first differential pressure value and the second height (H1) based on the mathematical formula:
• H1=aΔP1;
• a height (H2) of the solid bed existing at the upper pressure probe from the height arithmetic constant value (α) and the second differential pressure value (ΔP2) based on the mathematical formula:
• H2=aΔP2;
• and
• a height (HS) of the solid bed in a high-temperature and high-pressure fluidized bed system from the height (H2) of the solid bed existing at the upper pressure probe and the first height (H0) based on the mathematical formula:
• HS=H0+H2.

A solid bed height measuring method inside a fluidized bed reactor comprising:

• mounting a lower pressure probe at an upper side as high as a first height from a gas distributor of a fluidized bed reactor, mounting a middle pressure probe at an upper side as high as a second height from the lower probe and mounting an upper pressure probe at the top of the fluidized bed reactor, wherein the lower pressure probe and the middle pressure probe are mounted to exist inside the solid bed under all operation conditions, and the upper pressure probe is mounted at the upper side of the fluidized bed reactor, where the solid bed cannot reach, under all operation conditions;
• injecting fluidization gas into a gas introducing chamber below the gas distributor;
• measuring pressure values by the lower pressure probe, the middle pressure probe and the upper pressure probe;
• measuring a first differential pressure value (ΔP1), which is a differential pressure between a first pressure value measured by the lower pressure probe and a second pressure value measured by the middle pressure probe, and a second differential pressure value (ΔP2), which is a differential pressure between the first pressure value measured by the lower pressure probe and a third pressure value measured by the upper pressure probe, by a differential pressure type pressure converter;
• and
• operating a height arithmetic part for calculating a height of the solid bed inside the fluidized bed reactor based on the first differential pressure value (ΔP1) and the second differential pressure value (ΔP2), by at least
• calculating height arithmetic constant value (α)
• a
• =
• g
• c
• (
• 1
• -
• ɛ
• mf
• )
• ⁢
• (
• ρ
• s
• -
• ρ
• g
• )
• ⁢
• g
• (wherein εmf is a voidage of the solid bed under the minimum fluidization condition, ρs is density of the solid, μg is density of the gas, gc is a gravitational acceleration constant, and g is acceleration of gravity) from the first differential pressure value and the second height (H1) based on the mathematical formula:
• H1=aΔP1;
• a height (H2) of the solid bed existing at the upper pressure probe from the height arithmetic constant value (α) and the second differential pressure value (ΔP2) based on the mathematical formula:
• H2=aΔP2;
• and
• a height (HS) of the solid bed in a high-temperature and high-pressure fluidized bed system from the height (H2) of the solid bed existing at the upper pressure probe and the first height (H0) based on the mathematical formula:
• HS=H0+H2.