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

Patent metadata

Field	Value
Publication number	US-10415822-B2
Application number	US-201615133408-A
Country	US
Kind code	B2
Filing date	Apr 20, 2016
Priority date	Mar 17, 2016
Publication date	Sep 17, 2019
Grant date	Sep 17, 2019

Abstract

Disclosed are an apparatus and a method for measuring the height of a solid bed in a high-temperature and high-pressure fluidized bed system, and a fluidized bed system having the solid bed height measuring apparatus. The solid bed height measuring apparatus includes a lower pressure probe 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, and a middle pressure probe 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 is mounted at the top of the fluidized bed reactor to measure the inside pressure of the fluidized bed reactor. First and second differential pressure gauges are used for measuring differential pressures.

First claim

What is claimed is:

1. 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 first differential pressure gauge for measuring a first differential pressure value (ΔP 1 ) which is differential pressure between a first pressure value measured by the lower pressure probe and a second pressure value measured by the middle pressure probe;
a second differential pressure gauge for measuring a second differential pressure value (ΔP 2 ) which is differential pressure between a first pressure value measured by the lower pressure probe and a third pressure value measured by the upper pressure probe; 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 (ΔP 1 ) and the second differential pressure value (ΔP 2 ),
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, ρg 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 (H 1 ) on the basis of the mathematical formula:
H 1= aΔP 1;

a height (H 2 ) of the solid bed existing at the upper pressure probe from the height arithmetic constant value (α) and the second differential pressure value (ΔP 2 ) on the basis of the mathematical formula:
H 2= aΔP 2; and

a height (HS) of the solid bed in a high-temperature and high-pressure fluidized bed system from the height (H 2 ) of the solid bed existing at the upper pressure probe and the first height (H 0 ) on the basis of the mathematical formula
HS=H 0+ H 2.

2. The solid bed height measuring apparatus according to claim 1 , further comprising:
a display part for displaying the first pressure value, the second pressure value, the third pressure value, the first differential pressure value, the second differential pressure value and the height of the solid bed in real time.

3. 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 (ΔP 1 ) which is a differential pressure between the first pressure value and the second pressure value, and a second differential pressure value (ΔP 2 ) 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 (ΔP 1 ) and the second differential pressure value (ΔP 2 );
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 (H 1 ) based on the mathematical formula:
H 1= aΔP 1;

a height (H 2 ) of the solid bed existing at the upper pressure probe from the height arithmetic constant value (α) and the second differential pressure value (ΔP 2 ) based on the mathematical formula:
H 2= aΔP 2; and

a height (HS) of the solid bed in a high-temperature and high-pressure fluidized bed system from the height (H 2 ) of the solid bed existing at the upper pressure probe and the first height (H 0 ) based on the mathematical formula:
HS=H 0+ H 2.

4. The solid bed height measuring apparatus according to claim 3 , further comprising:
a display part for displaying the first pressure value, the second pressure value, the third pressure value, the first differential pressure value, the second differential pressure value and the height of the solid be

Assignees

• Korea Inst Energy Res

Inventors

• Ryu Ho-Jung
• Lee Dong-Ho
• Jin Gyoung-Tae
• Shun Do-Won
• Yi Chang-Keun
• Park Jae-Hyeon
• Bae Dal-Hee
• Jo Sung-Ho
• Lee Seung-Yong
• Park Young Cheol
• Moon Jong-Ho

Classifications

• F23C10/18 Primary

  Details; Accessories · CPC title

• F23C10/30

  for controlling the level of the bed or the amount of material in the bed · CPC title

• F23C10/16 Primary

  specially adapted for operation at superatmospheric pressures, e.g. by the arrangement of the combustion chamber and its auxiliary systems inside a pressure vessel · CPC title