Ammonia production plant and ammonia production method

Patent metadata

Field	Value
Publication number	US-11021373-B2
Application number	US-201816762605-A
Country	US
Kind code	B2
Filing date	May 11, 2018
Priority date	May 11, 2018
Publication date	Jun 1, 2021
Grant date	Jun 1, 2021

Abstract

An ammonia production plant includes an ammonia synthesis facility; a synthesis gas generating facility which generates a synthesis gas for synthesizing ammonia from the carbon-based raw material; and a power generating facility which obtains power. The synthesis gas generating facility includes an exhaust heat recovery unit which recovers exhaust heat. The power generating facility includes a combustion device which burns oxygen and fuel and a gas turbine which is driven by using a combustion gas containing a CO2 gas obtained by the combustion device as power so as to generate power and is configured to supply the CO2 gas discharged from the gas turbine as a recycle gas to the combustion device. The power obtained by the power generating facility powers the ammonia synthesis facility. The exhaust heat recovered by the exhaust heat recovery unit is used to heat the recycle gas.

First claim

The invention claimed is:

1. An ammonia production plant for producing ammonia from a carbon-based raw material, comprising:
an ammonia synthesis facility which synthesizes ammonia;
a synthesis gas generating facility which generates a synthesis gas for synthesizing ammonia from the carbon-based raw material; and
a power generating facility which obtains power,
wherein the synthesis gas generating facility includes an exhaust heat recovery unit which recovers exhaust heat generated when generating the synthesis gas,
wherein the power generating facility includes a combustion device which burns oxygen and fuel, and a gas turbine which is driven by using a combustion gas containing a CO 2 gas obtained by the combustion device as power so as to generate power and is configured to supply the CO 2 gas discharged from the gas turbine as a recycle gas to the combustion device,
wherein the power obtained by the power generating facility is used as at least power of the ammonia synthesis facility, and
wherein the exhaust heat recovered by the exhaust heat recovery unit is used to heat the recycle gas.

2. The ammonia production plant according to claim 1 ,
wherein the power generating facility includes a booster which supplies the CO 2 gas discharged from the gas turbine as the recycle gas to the combustion device,
wherein the synthesis gas generating facility is configured to recover the CO 2 gas contained in the synthesis gas, and
wherein the booster pressurizes the CO 2 gas discharged from the gas turbine and the recovered CO 2 gas.

3. The ammonia production plant according to claim 1 , further comprising:
a separation device which separates air into oxygen and nitrogen,
wherein the synthesis gas generating facility includes a first reforming unit which reforms the carbon-based raw material and a second reforming unit which reforms the carbon-based raw material not reformed by the first reforming unit,
wherein the second reforming unit is configured to reform the carbon-based raw material by a partial oxidation reaction, and
wherein the separation device is configured to supply oxygen to the combustion device and the second reforming unit.

4. The ammonia production plant according to claim 1 ,
wherein the exhaust heat recovery unit includes a high-temperature heat exchanger which recovers high-temperature exhaust heat having a predetermined temperature and a low-temperature heat exchanger which recovers low-temperature exhaust heat having a temperature lower than that of the high-temperature exhaust heat,
wherein the synthesis gas generating facility includes a first reforming unit which reforms the carbon-based raw material, a second reforming unit which reforms the carbon-based raw material not reformed by the first reforming unit, and a shift reaction unit which converts CO generated by a reforming reaction in the first reforming unit and the second reforming unit into CO 2 , and
wherein the high-temperature heat exchanger recovers the high-temperature exhaust heat generated in the second reforming unit and the low-temperature heat exchanger recovers the low-temperature exhaust heat generated in the shift reaction unit.

5. The ammonia production plant according to claim 4 ,
wherein the first reforming unit is configured to reform the carbon-based raw material by a water vapor reforming reaction, and
wherein a part of the high-temperature exhaust heat recovered by the high-temperature heat exchanger is used for the reforming reaction in the first reforming unit.

6. The ammonia production plant according to claim 4 ,
wherein the first reforming unit is configured to reform the carbon-based raw material by a water vapor reforming reaction, and
wherein a part of the low-temperature exhaust heat recovered by the low-temperature heat exchanger is used to generate water vapor necessary for at least the water vapor reforming reaction.

7. The ammonia production plant according to claim 1 ,
wherein the power generating facility includes a booster which supplies the CO 2 gas discharged from the gas turbine as the recycle gas to the combustion device,
wherein the exhaust heat recovered by the exhaust heat recovery unit is used to heat the CO 2 gas which is the CO 2 gas discharged from the gas turbine and will be supplied to the booster, and
wherein the recycle gas is heated by the heated CO 2 gas.

8. The ammonia production plant according to claim 1 ,
wherein the carbon-based raw material is a natural gas or coal.

9. An ammonia production plant for producing ammonia from a carbon-based raw material, comprising:
an ammonia synthesis facility which synthesizes ammonia;
a synthesis gas generating facility which generates a synthesis gas for synthesizing ammonia from the carbon-based raw material; and
a power generating facility which obtains power,
wherein the synthesis gas generating facility includes an exhaust heat recovery unit which recovers exhaust heat generated when generating the synthesis gas,
wherein the power generating facility includes a combustion device which burns oxygen and fuel, a water vapor generating device which generates water vapor by exhaust heat of a combustion gas containing a CO 2 gas obtained from the combustion device, and a steam turbine which is driven by using the water vapor generated in the water vapor generating device as power so as to generate power and is configured to supply the CO 2 gas discharged from the water vapor generating device as a recycle gas to the combustion device,
wherein the power obtained by the power generating facility is used as at least power of the ammonia synthesis facility, and
wherein the exhaust heat recovered by the exhaust heat recovery unit is used to generate water vapor in the water vapor generating device.

10. The ammonia production plant according to claim 9 ,
wherein the power generating facility includes a gas turbine which is driven by using the combustion gas as power so as to generate power and the water vapor generating device generates water vapor by exhaust heat of the gas turbine.

11. The ammonia production plant according to claim 10 ,
wherein the power generating facility includes a booster which supplies the CO 2 gas discharged from the gas turbine as the recycle gas to the combustion device,
wherein the synthesis gas generating facility is configured to recover the CO 2 gas contained in the synthesis gas, and
wherein the booster pressurizes the CO 2 gas discharged from the gas turbine and the recovered CO 2 gas.

12. The ammonia production plant according to claim 10 , further comprising:
a separation device which separates air into oxygen and nitrogen,
wherein the synthesis gas generating facility includes a first reforming unit which reforms the carbon-based raw material and a second reforming unit which reforms the carbon-based raw material not reformed by the first reforming unit,
wherein the second reforming unit is configured to reform the carbon-based raw material by a partial oxidation reaction, and
wherein the separation device is configured to supply oxygen to the combustion device and the second reforming unit.

13. The ammonia production plant according to claim 9 ,
wherein the exhaust heat recovery unit includes a high-temperature heat exchanger which recovers high-temperature exhaust heat having a predetermined temperature and a low-temperature heat exchanger which recovers low-temperature exhaust heat having a temperature lower than that of the high-temperature exhaust heat,
wherein the synthesis gas generating facility includes a first reforming unit which reforms the carbon-based raw material, a se

Assignees

• Jgc Corp

Inventors

• Fujimura Yasushi
• Kato Momoko

Classifications

• C01B2203/142

  At least two reforming, decomposition or partial oxidation steps in series · CPC title

• C01C1/0405

  from N2 and H2 in presence of a catalyst · CPC title

• C01B2203/0475

  the impurity being carbon dioxide · CPC title

• C01B2203/0261

  containing a catalytic partial oxidation step [CPO] · CPC title

• C01B2203/0844

  the non-combustive exothermic reaction being another reforming reaction as defined in groups C01B2203/02 - C01B2203/0294 · CPC title