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Device and process method for recovering synthetic ammonia tail gas to produce lng

A technology for synthesizing ammonia and tail gas, which is applied in the field of devices for recycling synthetic ammonia tail gas to produce LNG, which can solve the problems of inability to recycle, low economic benefits, environmental pollution, etc., and achieve the effects of compact structure, reduced energy consumption and operating costs, and reduced costs

Inactive Publication Date: 2016-08-17
杭州凯德空分设备有限公司
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  • Abstract
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Problems solved by technology

[0003] The most common way to deal with the tail gas of synthetic ammonia today is to discharge it directly into the atmosphere. However, the methane in the tail gas is a greenhouse gas, and its power to cause global warming is 25 times that of carbon dioxide, which causes environmental pollution and waste of resources. The other is to burn after collection and convert it into secondary energy such as heat energy and electric energy. However, the economic benefits of this method are low, and components such as methane and hydrogen with high economic added value in the tail gas cannot be recycled; Filtration and purification technology extracts methane and other valuable components in tail gas, but existing technologies and production processes have disadvantages such as high energy consumption, high cost, and low extraction rate

Method used

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  • Device and process method for recovering synthetic ammonia tail gas to produce lng

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Embodiment Construction

[0024] The present invention will be further described below with reference to the accompanying drawings.

[0025] Such as figure 1As shown, the coke oven raw gas riser sensible heat recovery device provided in this embodiment includes a circulating nitrogen compressor 7, a first cooler 8, a second cooler 9, a third cooler 10, and a Precooling heat exchange device 11, supercharged turbo expander, gas-liquid separator 14, dehydrogenation rectification tower 15 and methane rectification tower 16, said precooling heat exchange device 11 includes carbon dioxide precooler 1 and main Heat exchanger 2; the pre-cooling heat exchange device 11 is provided with a high-pressure tail gas inlet, a low-pressure tail gas inlet, a hydrogen-rich gas outlet, a nitrogen-rich gas outlet, a backflow cycle nitrogen outlet, a high-pressure nitrogen inlet, a high-pressure nitrogen outlet, and a backflow cycle nitrogen inlet , nitrogen-enriched gas inlet, hydrogen-enriched gas inlet, low-pressure tai...

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Abstract

The invention discloses a device and a technological method for producing LNG (liquefied natural gas) by recycling ammonia tail gas. The device comprises a circulation nitrogen compressor, a first cooler, a second cooler, a third cooler, a pre-cooling heat exchanging device, a booster expansion turbine, a gas-liquid separator, a dehydrogenation and distillation tower and a methane distillation tower, wherein the pre-cooling heat exchanging device, the booster expansion turbine, the gas-liquid separator, the dehydrogenation and distillation tower and the methane distillation tower are arranged in a cold box; and the pre-cooling heat exchanging device comprises a carbon dioxide pre-cooler and a main heat exchanger. The device and the technological method for producing the LNG by recycling the ammonia tail gas has the advantages that by an ammonia tail gas cryogenic separation technology, methane is extracted sufficiently while useful hydrogen produced by using ammonia is recycled, the methane is liquefied into LNG with high added value, the cost of ammonia is reduced, ammonia tail gas resources are sufficiently recycled, and the environment is protected.

Description

technical field [0001] The invention belongs to the technical field related to the recovery and utilization of exhaust gas (tail gas) in the ammonia synthesis industry, and particularly relates to a device and a process method for producing LNG from ammonia synthesis tail gas by cryogenically separating and extracting methane from synthesis ammonia tail gas into liquefied natural gas (LNG) . Background technique [0002] In the field of chemical fertilizer industry, the process of producing ammonia will produce a purge gas containing about 25% methane, and in the production process of synthetic ammonia, it will also produce a synthesis gas containing about 35% methane. The above gases constitute the tail gas of synthetic ammonia. In order to ensure the normal progress of the ammonia synthesis reaction, it is necessary to discharge the tail gas of synthetic ammonia to control the concentration of methane. [0003] The most common way to deal with the tail gas of synthetic am...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F25J3/02
Inventor 蔡福梅夏仕屔薄达吴志会潘翎周涛洪英华陈娟韩岭黄潞艇王涛平闫明松闫红伟陈剑军
Owner 杭州凯德空分设备有限公司
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