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Method and device for separating hydrogen and hydrocarbon in petroleum drying gas by using multi-stage cascade temperature-changing membrane

A membrane separation and petrochemical technology, applied in separation methods, chemical instruments and methods, hydrogen separation, etc., can solve problems such as high cost, few applications, and increased partial pressure of hydrocarbon components

Inactive Publication Date: 2010-12-08
魏伯卿
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] Now the commonly used separation methods in industry include cryogenic separation method, shallow cold separation method, oil product absorption method, adsorption method, membrane separation method and other methods; there are also methods combining these three or two methods at home and abroad. Patents (92109983.5, 200710131549.4, 200610135849.5 and 92100812.0, etc.), but they are rarely used in industry and the cost is relatively high
There are also patents (93103019.6, 95117302.2) using two-stage membrane separation and variable temperature two-stage membrane separation, but these patented technologies cannot separate mixed gas sources with relatively large hydrogen and hydrocarbon components, nor can they separate hydrogen content between 30% and 60%. Most of the hydrogen membrane separation devices that have been used in the industry are used to separate the mixed gas source with a hydrogen content of more than 60%; if the mixed gas source with a low hydrogen content and a high hydrocarbon content is separated, there will be liquid Hydrocarbons are precipitated in the second hydrogen membrane separation process
Because of the high hydrocarbon content, during the hydrogen separation process, with the separation and seepage of hydrogen, the partial pressure of the hydrocarbon components will increase, and the gaseous hydrocarbons will become liquid and precipitate in the membrane, which will damage the performance and use of the separation membrane. life

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  • Method and device for separating hydrogen and hydrocarbon in petroleum drying gas by using multi-stage cascade temperature-changing membrane
  • Method and device for separating hydrogen and hydrocarbon in petroleum drying gas by using multi-stage cascade temperature-changing membrane
  • Method and device for separating hydrogen and hydrocarbon in petroleum drying gas by using multi-stage cascade temperature-changing membrane

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Embodiment

[0023] Example: Separation and recovery of hydrogen hydrocarbons in petrochemical dry gas

[0024] The flow rate and composition of the mixed gas source provided by the user in the embodiment are shown in Attached Table 1, and the pressure of the mixed gas source provided is 0.5 Mpa (G);

[0025] User requirements: the concentration of recovered hydrogen should be above 85%, the recovery rate should be as high as possible, and the pressure of recovered hydrogen should be above 1.2MPa.

[0026] Using the process and calculation of the present invention: A, B, and C membranes are each equipped with one membrane, and the operating temperature of the three membranes is designed to be 55°C;

[0027] The 0.5 MPa (G) mixed gas source is compressed and boosted to 3.5 MPa (G), and the product hydrogen-rich gas pressure is 1.2 MPa (G).

[0028] The final available product hydrogen, that is, the mixed gas concentration of A membrane permeate gas + C membrane permeate gas is 85.73%, and ...

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Abstract

The invention relates to a method for separating hydrogen and hydrocarbon in a petroleum drying gas by using a multi-stage cascade temperature-changing membrane. In the method, after preprocessed, a mixed gas source firstly passes through a hydrogen separating membrane A for primarily separating partial hydrogen; seeped residual gas enters an organic gas separating membrane B for secondarily separating hydrocarbon components; and the seeped residual gas of the membrane B enters a hydrogen separating membrane C for thirdly separating the hydrogen. The invention also provides a device for separating low-concentration hydrogen in the petroleum drying gas by using the cascade membrane. The invention has the advantage that the organic gas separating membrane is arranged between the two hydrogen separating membranes for separating the hydrocarbon gases to ensure that liquid hydrocarbon is separated out during the secondary hydrogen membrane separation. Meanwhile, separating temperatures of the three separating membranes are calculated and the three membranes are configured by using an HYSYS and the hydrocarbon and hydrogen proportion in the mixed gas source, thereby ensuring that the membrane separating property and the membrane configuration are optimal.

Description

Technical field [0001] The present invention involves multi -level tandem temperature -transformed membrane to separate hydrocarbons in petrochemicals and its device. It is not only suitable for the industrialized and efficient separation of hydrocarbons in the dry gas of the refinery, but also applicable to other hybolized hybrids.Or the processing of hydrogen hydrocarbon, which is transformed into hydrogen -based hydrocarbons, is divided into efficient separation.It belongs to the field of gas separation technology. Background technique [0002] With the continuous development of the petrochemical industry, the continuous progress of processing and synthetic technology, the circulating gas, release gas and exhaust gas contained in the oil processing and chemical synthesis industries contain a large amount of hydrocarbon gases.Burning will be a great waste of resources and increasing industrial costs accordingly.A variety of valuable chemical raw materials such as ethylene, acry...

Claims

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Application Information

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IPC IPC(8): B01D53/22C01B3/50C10G70/04
Inventor 魏伯卿
Owner 魏伯卿