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Ammonia and carbon dioxide separation method

A carbon dioxide and separation method technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., can solve problems such as inability to separate, easy crystallization of ammonia and carbon dioxide, etc.

Active Publication Date: 2016-07-20
YASHENTECH CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] One object of the present invention is to provide a kind of separation method of ammonia and carbon dioxide, this separation method adopts absorption decarburization process, introduces potassium carbonate solution as absorbent, introduces low boiler in the absorption tower, improves carbon dioxide recovery rate, realizes ammonia, carbon dioxide The high-efficiency separation effectively solves the problem that ammonia and carbon dioxide are easy to crystallize and cannot be separated

Method used

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  • Ammonia and carbon dioxide separation method
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  • Ammonia and carbon dioxide separation method

Examples

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Embodiment 1

[0042] The first embodiment of the present invention relates to the process principle of a separation device for ammonia and carbon dioxide, as shown in the attached figure 1 As shown, the ammonia and carbon dioxide separation process includes: sending the mixed gas containing ammonia and carbon dioxide into a three-tower separation device including an absorption tower 1100, a recovery tower 1200 and a desorption tower 1300 for separation. First, the carbon dioxide absorption step is carried out in the absorption tower 1100: the mixed gas containing ammonia and carbon dioxide is sent into the absorption tower, and at the same time, a carbon dioxide absorbent (hereinafter also referred to as an absorbent) and low boilers are respectively introduced into the absorption tower, and the carbon dioxide absorbent Contains potassium carbonate solution; use a reboiler to heat the tower bottom of the absorption tower, extract ammonia-containing gaseous substances from the top of the abso...

Embodiment 2

[0048] The second embodiment of the present invention relates to a specific method and device for separating ammonia and carbon dioxide. as attached figure 2 As shown: the device for separating ammonia and carbon dioxide in this embodiment includes an absorption tower 2101, an absorption tower reboiler 2112, an absorption tower bottom discharge pump 2131, a recovery tower 2201, a recovery tower reboiler 2212, and a recovery tower condenser 2211, recovery tower reflux tank 2221, recovery tower reflux pump 2231, recovery tower tank discharge pump 2232, desorption tower 2301, desorption tower reboiler 2312, desorption tower condenser 2311, desorption tower reflux tank 2321, desorption tower reflux pump 2331, lean liquid circulating pump 2332, desorption tower kettle discharge cooler 2313.

[0049] In the lower part of the absorption tower 2101, there is a gas-phase feed inlet for the mixed gas to enter, in the upper end and middle part of the absorption tower 2101, there are ab...

Embodiment 3

[0055] The schematic diagram of the separation device involved in the third embodiment of the present invention is as attached image 3 As shown, the ammonia and carbon dioxide separation device of this embodiment is the same as that of Embodiment 2. The difference between the separation method of this embodiment and Embodiment 2 is that the mixed gas to be separated in this embodiment contains ammonia and carbon dioxide, but does not contain It can be used as a low boiler to participate in the components of the separation reaction. In addition, in this embodiment, methyl formate is selected as the low boiler. Specifically the separation method of the present embodiment is as follows:

[0056] The mixed gas of ammonia and carbon dioxide is sent to the middle and lower part of the absorption tower 3101. The absorption tower 3101 is a packed tower with an operating pressure of 0.2 MPa (A). The mass-liquid-gas ratio of the absorbent to the mixed gas is 3:1; the total alkalinity ...

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Abstract

The invention relates to an ammonia and carbon dioxide separation method. The method comprises the following steps: mixed gas containing ammonia and carbon dioxide is delivered into an absorption tower, and a carbon dioxide absorbent and a low-boiling-point substance are introduced; under the heating of a reboiler, ammonia-containing gaseous substance is recovered from the tower top, and a potassium bicarbonate rich liquor containing the low-boiling-point substance is obtained at the tower bottom; the potassium bicarbonate rich liquor containing the low-boiling-point substance is delivered into a recovery tower; the low-boiling-point substance is obtained at the tower top under the heating of a reboiler, and is recycled in the absorption tower; the potassium bicarbonate rich liquor with the low-boiling-point substance removed is obtained at the tower bottom; the potassium bicarbonate rich liquor with the low-boiling-point substance removed is delivered into a desorption tower; under the heating of a reboiler, carbon dioxide is obtained at the tower top, and potassium bicarbonate lean liquor is obtained at the tower bottom; the potassium bicarbonate lean liquor is returned to the absorption tower, and is reused as a carbon dioxide absorbent. With the ammonia-carbon dioxide separation method, a carbon dioxide recovery rate is close to 99.95%, and absorption tower bottom ammonia content is lower than 0.05%. Therefore, a problem of separation failure caused by the crystallization of ammonia and carbon dioxide is effectively solved.

Description

technical field [0001] The invention relates to the technical field of removing carbon dioxide in a mixture, in particular to a method for separating ammonia and carbon dioxide. Background technique [0002] A mixture of ammonia and carbon dioxide is produced during the production of urea or the synthesis of melamine from urea. How to efficiently separate ammonia and carbon dioxide from the mixed gas and make them as recycled materials or co-products / by-products plays a crucial role in the efficiency and economy of the production process. [0003] A special property of the mixture of ammonia and carbon dioxide is that, under normal pressure below about 59°C, the two tend to react spontaneously to form ammonium carbamate solid (Ammonium carbamate, referred to as methyl ammonium), which can easily lead to blockage of equipment and / or pipelines. However, since the boiling point of ammonia (-33°C under normal pressure) and carbon dioxide (-78°C under normal pressure) are far be...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/14C01B31/20C01B32/50
CPCY02C20/40Y02P20/10Y02P20/151Y02P20/50
Inventor 王讯文韩晖刘丹
Owner YASHENTECH CORP
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