Multi-level recycling pressure swing adsorption rapid oxygen-nitrogen generating device and method

A pressure swing adsorption and rapid technology, applied in the direction of oxygen preparation, separation methods, chemical instruments and methods, etc., can solve the problems of increased power total work, high cost of oxygen production, uncontrollable content, etc., to achieve long start-up time, reduce The effect of shortening power and time

CN108069400AActive Publication Date: 2018-05-25UNIV OF SHANGHAI FOR SCI & TECH
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Publication Date
2018-05-25

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Abstract

The invention relates to a multi-level recycling pressure swing adsorption rapid oxygen-nitrogen generating device and method. An oxygen purification system is connected a preliminary separation oxygen enrichment system through an oxygen enrichment high-pressure buffer tank T6, an oxygen enrichment middle-pressure buffer tank T5 and an oxygen enrichment low-pressure buffer tank T4, and is connected with a gas drying and purifying system through a high-purity oxygen acceleration pipe and a drying and purifying tail gas recovering pipe. An oxygen enrichment tail gas of the oxygen purification system is partially recovered and used as a regeneration gas of the gas drying and purifying system, and the regeneration gas of the gas drying and purifying system is partially recovered and used as anair source. The gas drying and purifying system is connected with an air inlet buffer tank T1 through a compressed air purifying system and a compressor CP1. The air separation raw material components of the device are adjusted by controlling the suction volume of the clean air of the air inlet buffer tank, and the efficiency of purifying the oxygen is improved. A multi-level tail gas recovery technology, a gas compression work recovery technology and a multi-step pressure-equalizing and flow control technology are used for realizing the low energy consumption while the high-quality nitrogenand oxygen are generated, and effectively shortening the available machine time.
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Description

technical field

[0001] The present invention relates to an air separation mechanical device, and more specifically, to a device and method for rapidly producing high-quality oxygen and nitrogen by pressure swing adsorption air separation based on multi-stage recovery. Background technique

[0002] The pressure swing adsorption air separation technology mainly relies on the different adsorption capacity of the adsorbent for each component gas in the air under different pressures to achieve the purpose of separating each component gas.

[0003] PSA uses clean air as raw material, its energy consumption basically comes from the power consumption of the compressor, and the production cost basically comes from the energy consumption cost. How to effectively improve the gas production capacity per unit of total compression work is the core direction of technology research and development. For For conventional pressure swing adsorption air separation nitrogen and oxygen production ...

Examples

Embodiment Construction

[0023] The drawings constituting a part of the present invention are used to provide a further understanding of the present invention, and the schematic embodiments and descriptions of the present invention are used to explain the present invention, and do not constitute an improper limitation of the present invention. In the attached picture. In order to better understand the present invention, the present invention will be further described below in conjunction with specific examples.

[0024] like figure 1 The shown equipment for rapid production of high-quality oxygen and nitrogen based on multi-stage recovery pressure swing adsorption air separation mainly includes air filter 1, air inlet solenoid valve SV1 2, air inlet buffer tank T1 3, compressor CP1 4, Compressed air purification system 5, gas drying and purification system 52, oxygen-enriched purification tail gas recovery tank T2 46, buffer tank T3 45 after drying, high-purity oxygen speed-up pipeline 12, solenoid v...