US20020014419A1 - Ozone storing method and ozone extracting method - Google Patents

Ozone storing method and ozone extracting method Download PDF

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Publication number
US20020014419A1
US20020014419A1 US09/915,535 US91553501A US2002014419A1 US 20020014419 A1 US20020014419 A1 US 20020014419A1 US 91553501 A US91553501 A US 91553501A US 2002014419 A1 US2002014419 A1 US 2002014419A1
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United States
Prior art keywords
ozone
silica gel
storage container
water
storage
Prior art date
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Abandoned
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US09/915,535
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English (en)
Inventor
Akira Murai
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Kansai Electric Power Co Inc
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Individual
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Filing date
Publication date
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Assigned to KANSAI ELECTRIC POWER CO., INC., THE reassignment KANSAI ELECTRIC POWER CO., INC., THE ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MURAI, AKIRA
Publication of US20020014419A1 publication Critical patent/US20020014419A1/en
Abandoned legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/10—Preparation of ozone

Definitions

  • the present invention relates to a method of storing ozone that has been produced and a method of extracting the stored ozone for a desired use.
  • ozone is stored in a cooled adsorbent by applying pressure and then to extract the ozone, the adsorbent is heated and/or an ozone storage container containing the adsorbent is decompressed.
  • the ozone storage container is filled with a silica gel, which is cooled to a temperature between ⁇ 30° C. and ⁇ 60° C., and then the ozone is supplied with pressure so as to be adsorbed in the cooled silica gel.
  • the silica gel contained in the ozone storage container is heated and also the inside of the storage container is decompressed.
  • an adsorbent is cooled to a temperature lower than ⁇ 30° C. by a cooling means such as refrigeration device and then ozone is supplied with pressure to the adsorbent so that the ozone can be stored in the adsorbent.
  • a cooling means such as refrigeration device
  • ozone is supplied with pressure to the adsorbent so that the ozone can be stored in the adsorbent.
  • the adsorbent is heated and/or decompressed.
  • the adsorbent is cooling when it adsorbs ozone and it is heating when it desorbs ozone. Therefore, this method causes a drastic change in temperature for the adsorbent and as a result, the durability of the adsorbent deteriorates.
  • this method requires a large amount of energy for electricity.
  • the storage container is supplied with pressure so as to allow pressurizing up to 5 atm. when the adsorbent adsorbs ozone and it is decompressing to 0.04 atm. when the ozone is discharged.
  • this pressurizing step causes a significant cost increase because a large-scale apparatus and additional works are required. Furthermore, a large amount of space is required to install such an ozone storage apparatus. For these reasons, there are many problems to be solved before widespread use of an ozone storage apparatus is acceptable.
  • Another concern relates to the characteristics of the silica gel in an ozone storage mechanism.
  • silica gel has characteristics such that the amount of gas adsorbed in silica gel increases in proportion to the surface area.
  • silica gel does not exhibit this characteristic with ozone. This means that ozone is not simply adsorbed in silica gel by surface adsorption, but rather it is adsorbed by another mechanism.
  • silica gel when the silica gel adsorbs ozone, it is necessary to use silica gel that is suitable for the ozone adsorbing mechanism. It is also necessary to use storing and extracting methods that are appropriate to the ozone adsorbing mechanism.
  • an object of the present invention is to provide ozone storage/extraction methods appropriate to the ozone storing characteristics of the silica gel.
  • the ozone when ozone is supplied to a silica gel, the ozone is isothermally compressed in the micropores of the silica gel and a part of the ozone is liquefied in the silica gel.
  • the inventor has determined efficient ozone storage/extraction methods based on consideration of this ozone storage mechanism.
  • the micropores of a silica gel need to be maintained in certain dimensions.
  • the micropores of a silica gel either are melted by an excessive washing with water after the silica gel is neutralized, or when the water solvent evaporates, the silica gel cracks and the micropores of the silica gel collapse.
  • the present invention is directed to an ozone storage/extraction method and apparatus where silica gel produced by a neutralization of an alkaline silicate under a weak acid to a pH level between 6 and 7 is dried and then used, or the dried silica gel is further crushed and washed with sulfuric acid or water.
  • a crushed silica gel increases the surface area of the substance, so this effort makes the speed of adsorption/desorption faster than the original silica gel.
  • the silica gel includes 0.002-0.1 percent by weight of aluminum.
  • oxygen is supplied so as to be adsorbed in the silica gel and then the oxygen is evacuated. Thereafter, the ozone is supplied to the silica gel.
  • the present invention uses diffusion dependent on the different concentrations of ozone between the outside of the silica gel and the surface of the capillary, and then uses the downward flow of the ozone caused by gravity.
  • ozone is extracted from the silica gel by heating and/or by decompressing so as to vaporize the ozone.
  • the inventor has evaluated that ozone storage in a silica gel goes through an isothermal compressing process and that ozone is becoming a cluster when it is stored in the silica gel.
  • An ozone extraction method utilizes the diffusion of ozone and the downward flow by gravity.
  • ozone is stored in an ozone storage container filled with the silica gel and a tube-valve located in the lower part of the ozone storage container is opened.
  • a tube-valve located in the lower part of the ozone storage container is opened.
  • oxygen is supplied through another opening that is located in the upper part of the ozone storage container at a rate adjusted to the downward flow rate of the ozone. Accordingly, a natural downward flow of ozone can be achieved.
  • FIG. 1 is a schematic diagram showing the structure of an ozone storage apparatus according to the present invention.
  • FIGS. 2 A- 2 D are schematic diagrams showing the ozone storage/extraction structure according to the present invention.
  • FIG. 3 is another schematic diagram showing the modified structure of an ozone storage apparatus according to the present invention.
  • the ozone storage apparatus shown in FIG. 1 comprises an oxygen supply source 1 , an ozone generating device 2 , a vacuum pump 5 , an ozone storage container 6 and a silica gel 7 .
  • the oxygen supply source 1 and the ozone generating device 2 are connected by a pipe so as to supply oxygen from the oxygen supplying source 1 to the ozone generating device 2 .
  • the ozone produced by the ozone generating device 2 is introduced into the ozone storage container 6 through another pipe.
  • a two-way valve 3 and a valve 4 are located in the flow path of the pipe connecting the ozone generating device 2 and the ozone storage container 6 .
  • pipes are connected to an upper part and a lower part of the ozone storage container 6 , respectively.
  • a valve 8 is located in the pipe connected to the lower part of the ozone storage container 6 .
  • silica gel capable of storing ozone a silica gel that is suitable for isothermally compressing ozone in the micropores thereof is used.
  • Such silica gel is produced by a method comprising the steps of neutralizing sodium silicate and sulfuric acid to produce a silica gel and washing the silica gel with water to a pH level between 6 and 7. In this procedure, it is important to avoid excessive washing with water to prevent the micropores from collapsing or melting in this water-washing step. This is also important to keep the sulfuric acid in the silica gel.
  • the silica gel is dried and then used or it is further treated and crushed and washed with sulfuric acid or water.
  • the concentration of sulfuric acid should be 0.1-5 percent by weight and the silica gel should be washed for 1-2 hours. Washing the silica gel with sulfuric acid allows the sulfuric acid to remain in the silica gel and thereby the micropores in the silica gel can be prevented from collapsing when it is dried.
  • the silica gel including 0.002-0.1 percent by weight of aluminum is used as a storage medium.
  • the silica gel 7 capable of adsorbing and storing ozone is evacuated after oxygen has been adsorbed therein. This is done to remove nitrogen that has been adsorbed in the silica gel. By removing the nitrogen from the silica gel, the amount of ozone adsorbed in the silica gel increases.
  • the ozone storage container 6 needs to be evacuated after oxygen has been supplied to the silica gel 7 as a preliminary process prior to supplying ozone to be adsorbed in the silica gel.
  • valves 4 and 8 are opened to introduce ozone into the ozone storage container 6 from the ozone generating device 2 and thereby ozone is adsorbed in the silica gel 7 . Since ozone is supplied through the valve located in the upper part of the ozone storage container 6 , ozone initially starts to be adsorbed in the adsorbent in the upper portion of the ozone storage container 6 . As shown in FIG. 2A, an adsorbed ozone region 7 b of the silica gel appears in an upper portion of the ozone storage container 6 . Then, as shown in FIG. 2B, by continuously supplying ozone, the ozone adsorbed region extends throughout the entire silica gel 7 in the ozone storage container 6 .
  • an ozone concentration monitor is located in the inside lower part of the ozone storage container 6 . It is also possible to judge whether a sufficient amount of ozone is stored in the ozone storage container 6 from the color of the silica gel based on the fact that the silica gel turns to blue when ozone is adsorbed.
  • valves 4 and 8 are opened and oxygen is supplied into the ozone storage container 6 .
  • a rate of oxygen supply should be adjusted to be substantially similar to a natural downward flow rate of ozone.
  • one supplying rate of oxygen is 200 ml/min for a 1-liter storage container.
  • ozone stored in the ozone storage container 6 can be extracted without hindering the natural downward flow of ozone.
  • the ozone stored in silica gel under low pressure for example 1.0-5.0 atm. and preferably 1.0-1.1 atm.
  • the inventor has determined that the best way to extract the clathrated ozone in the cluster state is by using a natural downward flow of ozone.
  • the ozone in this cluster state shows strong oxidizing and decomposing characteristics and thus by maintaining the ozone in this cluster state, the oxidizing and decomposing abilities of the ozone can be improved.
  • ozone can be stored efficiently by using the method disclosed in this invention. Further, by using the method of the present invention, the ozone in the cluster state can be extracted, thereby oxidation decomposition using ozone can be performed efficiently.
  • the present invention can simplify the structure of ozone storage apparatus and also improve the durability of the ozone storage apparatus.
  • FIG. 3 shows a modified ozone storage apparatus similar to FIG. 1 that uses the same reference numeral for the same elements.
  • This apparatus similarly comprises an oxygen supply source 1 , an ozone generating device 2 , a vacuum pump 5 , an ozone storage container 6 and a silica gel 7 .
  • the oxygen supply source 1 and the ozone generating device 2 are connected by a pipe so as to supply oxygen from the oxygen supplying source 1 to the ozone generating device 2 .
  • the ozone produced by the ozone generating device 2 is introduced into the ozone storage container 6 through another pipe.
  • a two-way valve 3 and a valve 4 are located in the flow path of the pipe connecting the ozone generating device 2 and the ozone storage container 6 .
  • pipes are connected to an upper part and a lower part of the ozone storage container 6 , respectively.
  • a valve 8 is located in one of the pipes connected to the lower part of the ozone storage container 6 .
  • a tube-valve 18 is located in the other pipe connected to the lower part of the ozone storage container 6 .
  • a tube-valve 14 is located in one of the pipes connected to the upper part of the ozone storage container.
  • valves 4 and 8 can be used to extract ozone from the container 6 .
  • FIG. 3 it is also possible to extract ozone from the container 6 using the tube-valves.
  • valves 4 and 8 can be used to fill the container with ozone as described above and the tube-valves can be used to extract the ozone.
  • oxygen can be supplied to the container 6 through tube-valve 14 .
  • the advantage of using the tube valves is that the ozone can be extracted through the lower tube-valve 18 without applying pressure by opening the upper and lower tube-valves.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
US09/915,535 2000-07-27 2001-07-27 Ozone storing method and ozone extracting method Abandoned US20020014419A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2000-227127 2000-07-27
JP2000227127A JP4491118B2 (ja) 2000-07-27 2000-07-27 オゾンの取出方法

Publications (1)

Publication Number Publication Date
US20020014419A1 true US20020014419A1 (en) 2002-02-07

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US09/915,535 Abandoned US20020014419A1 (en) 2000-07-27 2001-07-27 Ozone storing method and ozone extracting method

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US (1) US20020014419A1 (ja)
EP (1) EP1176118A1 (ja)
JP (1) JP4491118B2 (ja)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050274125A1 (en) * 2004-06-09 2005-12-15 Giacobbe Frederick W Methods of dissolving ozone in a cryogen
CN109437112A (zh) * 2018-12-28 2019-03-08 项义考 一种利用浓硫酸为干燥剂的臭氧用气体干燥器

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4803026B2 (ja) * 2006-12-28 2011-10-26 トヨタ自動車株式会社 内燃機関の排気ガス浄化装置
CN103754829B (zh) * 2014-01-27 2015-10-28 蹇守民 一种氧气和臭氧分离的方法
JP6545964B2 (ja) * 2015-01-26 2019-07-17 株式会社オーク製作所 エキシマランプ装置
CN117616275A (zh) * 2021-07-21 2024-02-27 三菱电机株式会社 臭氧量计算装置、臭氧贮藏容器及剩余臭氧量计算方法

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS601115A (ja) * 1983-06-16 1985-01-07 Central Glass Co Ltd 透明歯磨用非晶質シリカおよびその製造方法
JPH0699133B2 (ja) * 1985-12-18 1994-12-07 東ソー株式会社 液体クロマトグラフイ−用シリカゲルの製造方法
JP3622997B2 (ja) * 1994-09-05 2005-02-23 富士シリシア化学株式会社 シリカキセロゲルの製造方法
JP3316325B2 (ja) * 1994-12-20 2002-08-19 富士シリシア化学株式会社 ビール安定化処理用シリカゲル及びその製造方法並びにビールの安定化処理方法
JPH10196893A (ja) * 1997-01-14 1998-07-31 Iwatani Internatl Corp オゾンの取出方法
JPH10196890A (ja) * 1997-01-14 1998-07-31 Iwatani Internatl Corp オゾンガスの貯蔵方法
JPH1143307A (ja) * 1997-07-24 1999-02-16 Mitsubishi Electric Corp オゾン製造装置
JP3434197B2 (ja) * 1998-04-03 2003-08-04 三菱重工業株式会社 オゾン吸着剤、オゾン吸着用成形体及びその製造方法
JP2000203807A (ja) * 1999-01-19 2000-07-25 Nippon Sanso Corp 高濃度オゾンの供給方法及び装置
JP3091191B1 (ja) * 1999-07-08 2000-09-25 関西電力株式会社 オゾンの貯蔵改質方法および装置
JP4443738B2 (ja) * 2000-07-27 2010-03-31 関西電力株式会社 オゾン貯蔵用シリカゲルの調製方法

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050274125A1 (en) * 2004-06-09 2005-12-15 Giacobbe Frederick W Methods of dissolving ozone in a cryogen
US7392657B2 (en) 2004-06-09 2008-07-01 American Air Liquide, Inc. Methods of dissolving ozone in a cryogen
CN109437112A (zh) * 2018-12-28 2019-03-08 项义考 一种利用浓硫酸为干燥剂的臭氧用气体干燥器

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JP4491118B2 (ja) 2010-06-30
EP1176118A1 (en) 2002-01-30
JP2002037610A (ja) 2002-02-06

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Owner name: KANSAI ELECTRIC POWER CO., INC., THE, JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MURAI, AKIRA;REEL/FRAME:014339/0220

Effective date: 20010719

STCB Information on status: application discontinuation

Free format text: EXPRESSLY ABANDONED -- DURING EXAMINATION