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Device and method for deep removing water and carbon dioxide in nitrous oxide

A technology of nitrous oxide and carbon dioxide, which is applied in the field of chemical production, can solve the problems of unable to meet the purity requirements and improve the adsorption performance of the adsorbent, and achieve the effect of improving the adsorption performance, increasing the adsorption speed, and increasing the adsorption depth

Active Publication Date: 2014-11-12
中昊光明化工研究设计院有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Chinese Patent CN1827524A "Electronic Grade Laughing Gas Purification Process", this patent is to produce electronic grade laughing gas through chemical purification and molecular sieve purification, but the purification process working pressure It is 0.3-1.0MPa, which belongs to low-pressure adsorption. Under this process condition, the adsorption performance of the adsorbent cannot be improved
Moreover, the technical indicators of the products produced by this process do not mention the water as the key impurity in electronic-grade nitrous oxide. The carbon dioxide content is 2PPm, which is also at a relatively high level. Gas Nitrous Oxide" (GB / T 14600-2009) and the technical indicators of similar foreign products are quite different, and it has been unable to meet the purity requirements of the existing high-purity (electronic gas) nitrous oxide used in the electronics industry

Method used

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  • Device and method for deep removing water and carbon dioxide in nitrous oxide

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Put the raw material bottle 2 containing 25Kg nitrous oxide into the heater 1, heat the heater 1 to a temperature of 25°C, and when the pressure of the raw material bottle 2 reaches 2.0 MPa, open the first pressure reducing valve 3 to make the raw material gas flow along the gas pipeline (11) Enter the 13X molecular sieve adsorber (4), 5A molecular sieve adsorber (5), modified molecular sieve adsorber (6) and 3A molecular sieve adsorber (7) in sequence for adsorption and removal of impurities. When the pressure in the adsorber reaches 2.0MPa, open the second decompression valve 8, control the adsorber pressure to be 2.0MPa all the time, collect the product bottle temperature at -100--140°C, and collect 5Kg of product. The impurity contents of water and carbon dioxide in the collected nitrous oxide products are H 2 O2 <1PPm.

Embodiment 2

[0023]Put the raw material bottle 2 containing 25Kg of nitrous oxide into the heater 1, heat the heater 1 to a temperature of 25°C, and when the pressure of the raw material bottle 2 reaches 3.0 MPa, open the first pressure reducing valve 3 to make the raw material gas flow along the gas pipeline (11) Enter the 13X molecular sieve adsorber (4), 5A molecular sieve adsorber (5), modified molecular sieve adsorber (6) and 3A molecular sieve adsorber (7) in sequence for adsorption and removal of impurities. When the pressure in the adsorber reaches 3.0MPa, the second pressure reducing valve 8 is opened to control the pressure of the adsorber to be 3.0MPa all the time. The temperature of the collected product bottle is -100--140°C, and 5Kg of product is collected. The impurity contents of water and carbon dioxide in the collected nitrous oxide products are H 2 O2 <1PPm.

Embodiment 3

[0025] Put the raw material bottle 2 containing 25Kg of nitrous oxide into the heater 1, heat the heater 1 to a temperature of 25°C, and when the pressure of the raw material bottle 2 reaches 4.0MPa, open the first pressure reducing valve 3 to make the raw material gas flow along the gas pipeline (11) Enter the 13X molecular sieve adsorber (4), 5A molecular sieve adsorber (5), modified molecular sieve adsorber (6) and 3A molecular sieve adsorber (7) in sequence for adsorption and removal of impurities. When the pressure in the adsorber reaches 4.0MPa, the second pressure reducing valve 8 is opened to control the pressure of the adsorber to be 4.0MPa all the time. The temperature of the collected product bottle is -100--140°C, and 5Kg of product is collected. The impurity contents of water and carbon dioxide in the collected nitrous oxide products are H 2 O2 <1PPm.

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Abstract

The invention discloses a device and method for deep removing water and carbon dioxide in nitrous oxide, and belongs to the technical field of chemical industry production. The device comprises a raw material bottle, a collecting bottle and adsorbing devices. The adsorbing devices include the 13X molecular sieve adsorbing device, the 5A molecular sieve adsorbing device, the modified molecular sieve adsorbing device and the 3A molecular sieve adsorbing device, wherein the 13X molecular sieve adsorbing device, the 5A molecular sieve adsorbing device, the modified molecular sieve adsorbing device and the 3A molecular sieve adsorbing device are sequentially connected. The raw material bottle is heated by a heating device on the outer side of the raw material bottle, a first pressure reducing device is opened when the pressure of raw gas in the raw material bottle reaches 2.0 MPa to 4.0 MPa, and the raw gas sequentially enters the molecular sieve adsorbing devices. When the pressure of the gas in the adsorbing devices reaches 2.0 MPa to 4.0 MPa, a second pressure reducing device is opened, and the gas with impurities removed through the adsorbing devices is collected into the collecting bottle, wherein a refrigerating device is arranged on the outer side of the collecting bottle. By means of the method, the adsorbing depth and the adsorbing speed of adsorbents are increased through high-pressure adsorption, the physical adsorbing function and the chemical reaction function are achieved by conducting chemical modification on molecular sieves, the adsorbing performance of the adsorbents is improved, the water impurity and the carbon dioxide impurity in the nitrous oxide are deep removed, and a high-purity nitrous oxide product is obtained.

Description

technical field [0001] The invention relates to a device and method for deep removal of water and carbon dioxide in nitrous oxide, belonging to the technical field of chemical production. Background technique [0002] Nitrous oxide (N 2 O) is commonly known as laughing gas, and its chemical name is nitrous oxide. In the production process of microelectronics and optoelectronic devices, from the growth of the chip to the packaging of the final device, almost every step and every link is inseparable from the electron gas. Therefore, the electron gas is called the "food" and "source" of semiconductor materials. . The performance of semiconductor devices depends to a large extent on the quality of the electron gas used. Every order of magnitude increase in the purity of the electron gas will greatly promote the leap in the quality of semiconductor devices. Since the quality of electronic gas determines the development of IC technology, and semiconductor devices are widely use...

Claims

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Application Information

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IPC IPC(8): C01B21/22B01D53/02
CPCY02C20/10Y02P20/151
Inventor 高天龙牛永进梁肃臣
Owner 中昊光明化工研究设计院有限公司
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