Urea manufacturing method and urea manufacturing apparatus

Patent metadata

Field	Value
Publication number	US-10604477-B2
Application number	US-201615758295-A
Country	US
Kind code	B2
Filing date	Aug 31, 2016
Priority date	Sep 8, 2015
Publication date	Mar 31, 2020
Grant date	Mar 31, 2020

Abstract

Provided are urea manufacturing method and apparatus, which can increase the conversion ratio into urea and to reduce the consumption of steam. The temperature of the reactor is increased by introducing the entire amount of raw material ammonia and introducing a portion of the decomposed gas from the stripper into the reactor. The raw material ammonia is preferably heated using the steam condensate generated in the purification step, and/or the steam generated by the heat of condensation of the decomposed gas and the unreacted substances in the condensation step. The heating temperature is preferably between 70 and 140° C.

First claim

The invention claimed is:

1. A urea manufacturing method comprising:
an ammonia introduction step of introducing an entire amount of raw material ammonia directly into a reactor;
a synthesis step of reacting carbon dioxide and ammonia under a condition of excessive ammonia in the reactor, thereby providing a synthesis mixture containing urea, ammonium carbamate, water, unreacted ammonia, and unreacted carbon dioxide;
a decomposition step of decomposing the ammonium carbamate by heating the synthesis mixture and stripping using at least a portion of raw material carbon dioxide as an auxiliary agent in a stripper, thereby providing a decomposed gas containing ammonia and carbon dioxide, and a urea synthesis solution containing ammonia, carbon dioxide, water, and urea;
a purification step of separating water and unreacted substances including ammonia and carbon dioxide from the urea synthesis solution in a purification system, thereby providing a purified urea solution and recovering the separated water and unreacted substances;
a decomposed gas introduction step of introducing a portion of the decomposed gas provided in the stripper directly into the reactor via an ejector which uses the entire amount of the raw material ammonia as a driving fluid;
a condensation step of condensing the rest of the decomposed gas with at least a portion of the water and unreacted substances recovered in the purification step in a condenser, thereby providing a condensate and uncondensed gas, separately;
an off gas returning step for returning the uncondensed gas obtained in the condenser to the purification system; and
a condensate introduction step of introducing the condensate to the reactor using the ejector for introducing the condensate to the reactor.

2. The method according to claim 1 , wherein the raw material ammonia is heated in the ammonia introduction step using a steam condensate generated in the purification step and/or a steam generated by heat of condensation in the condensation step.

3. The method according to claim 1 , wherein the raw material ammonia is heated up to from 70 to 140° C. in the ammonia introduction step.

4. The method according to claim 1 , wherein between 5 and 20 wt % of the decomposed gas is introduced into the reactor in the decomposed gas introduction step.

5. The method according to claim 1 , wherein the condenser is a shell and tube condenser, and wherein the decomposed gas from the stripper and the unreacted substances from the purification system are introduced to the shell side of the condenser.

6. The method according to claim 5 , wherein the condenser is a bubble column vertical condensation reactor.

7. The method according to claim 1 , further comprising:
a carbon dioxide introduction step of introducing a part of raw material carbon dioxide directly into the reactor and the rest of the raw material carbon dioxide directly into the stripper, using a carbon dioxide introduction line that is directly connected to the reactor and the stripper.

8. A urea manufacturing apparatus comprising:
a reactor in which carbon dioxide and ammonia are reacted under a condition of excessive ammonia, thereby providing a synthesis mixture containing urea, ammonium carbamate, water, unreacted ammonia, and unreacted carbon dioxide;
an ammonia introduction line that is used to introduce an entire amount of raw material ammonia directly into the reactor;
a stripper that decomposes the ammonium carbamate by heating the synthesis mixture and stripping using at least a portion of raw material carbon dioxide as an auxiliary agent, thereby providing a decomposed gas containing ammonia and carbon dioxide, and a urea synthesis solution containing ammonia, carbon dioxide, water, and urea;
a purification system that purifies urea by separating water and the unreacted substances including ammonia and carbon dioxide from the urea synthesis solution, and recovers the separated water and unreacted substances;
a decomposed gas introduction line that is used to introduce a portion of the decomposed gas provided in the stripper directly into the reactor, wherein the decomposed gas introduction line is connected to an ejector and the decomposed gas is introduced to the reactor via the ejector, which uses the entire amount of the raw material ammonia as a driving fluid;
a condenser that condenses the rest of the decomposed gas with at least a portion of the water and unreacted substances recovered in the purification system, thereby providing a condensate and uncondensed gas, separately;
an off gas line for returning the uncondensed gas obtained in the condenser to the purification system; and
a condensate introduction line that is used to introduce the condensate to the reactor using the ejector for introducing the condensate to the reactor.

9. The apparatus according to claim 8 , wherein the raw material ammonia can be heated in the ammonia introduction line using a steam condensate generated in the purification and/or steam generated in the condenser.

10. The apparatus according to claim 8 , wherein the condenser is a shell and tube condenser, and wherein the decomposed gas from the stripper and the unreacted substances from the purification system are introduced to the shell side of the condenser.

11. The apparatus according to claim 10 , wherein the condenser is a bubble column vertical condensation reactor.

12. The apparatus according to claim 8 , further comprising:
a carbon dioxide introduction line that is directly connected to the reactor and the stripper and that is used to introduce a part of raw material carbon dioxide directly into the reactor and the rest of the raw material carbon dioxide directly into the stripper.

Assignees

• Toyo Engineering Corp

Inventors

• Sato Keishi
• Yoshimoto Kenji
• Morikawa Haruyuki

Classifications

• C07C273/16

  Separation; Purification · CPC title

• C07C273/04 Primary

  from carbon dioxide and ammonia · CPC title

• B01D3/009

  in combination with chemical reactions · CPC title

• C07C275/00

  Derivatives of urea, i.e. compounds containing any of the groups [IMAGE cpc-sch-C07C-0967.gif], the nitrogen atoms not being part of nitro or nitroso groups · CPC title

• B01D5/0081

  Feeding the steam or the vapours · CPC title