JP2003126681A - Carbon dioxide as energy carrier and use of the same - Google Patents
Carbon dioxide as energy carrier and use of the sameInfo
- Publication number
- JP2003126681A JP2003126681A JP2001363459A JP2001363459A JP2003126681A JP 2003126681 A JP2003126681 A JP 2003126681A JP 2001363459 A JP2001363459 A JP 2001363459A JP 2001363459 A JP2001363459 A JP 2001363459A JP 2003126681 A JP2003126681 A JP 2003126681A
- Authority
- JP
- Japan
- Prior art keywords
- carbon dioxide
- gas
- dry ice
- energy carrier
- pressurized
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
Abstract
Description
【0001】[発明の属する技術分野]全て既知の技術
の集約による環境、省エネに属する技術分野[Technical field to which the invention belongs] Technical field related to environment and energy saving by integrating all known technologies
【0002】[従来の技術]発電量は主に酷暑の節、冷
房機のフル回転時に最高値を示すこれまではその必要量
に応じ発電量を増やし辛うじて停電等の問題を起こすこ
とは無かったが、IT革命によりコンピユーターのハー
ド機器の冷却のための電力が常用電力量を押し上げるの
で、今後は更なる発電機の増設が求められるが、原子力
発電は設置場所の決定が困難、石油、天然ガス発電は二
酸化炭素の排出増加の問題を抱えている。[Prior Art] The amount of power generation is mainly at the time of extreme heat and shows the maximum value at the time of full rotation of the air conditioner. Until now, the amount of power generation was increased according to the required amount, and there was no problem such as power failure. However, due to the IT revolution, the electric power for cooling the computer's hard equipment will increase the amount of regular electric power, so it is necessary to add more generators in the future, but it is difficult to decide the installation location for nuclear power generation, oil, natural gas. Power generation suffers from increased carbon dioxide emissions.
【0003】[発明が解決しようとする課題]常用発電
量と最高発電量の差を縮小するのが唯一の課題であるが
太陽光発電は個人的に有用でも今日国家補助金を提供し
ても価格的に普及に手間取っている、またコジェネレー
ターにしても結構な二酸化炭素排出量を伴う。[PROBLEMS TO BE SOLVED BY THE INVENTION] The only problem is to reduce the difference between the normal power generation amount and the maximum power generation amount. However, even if solar power generation is personally useful or provides a national subsidy today. It takes time to spread the price, and even with a co-generator, it has a considerable amount of carbon dioxide emissions.
【0004】[課題を解決するための手段]発電量の最
低になる低額な深夜電力乃至余剰電力を利用しエネルギ
ー担体を作り、そのエネルギーを昼間の発電エネルギー
に変換出来れば理想的な解決法の一つになり、既に圧搾
空気を岩塩ドームに保存し、昼間の発電に利用した例が
あるが、収納場所に問題があり一般的でない。本発明は
移動も可能な、小容積で保存も容易なエネルギー担体を
低額な電力で作り、昼間、夜間を問わず任意の場所での
発電エネルギーとして提供できる。[Means for Solving the Problem] If an energy carrier is made by using low-cost late-night power or surplus power that produces a minimum amount of power generation, and the energy can be converted into daytime power generation energy, it is an ideal solution. There is an example in which compressed air is already stored in a salt dome and used for power generation in the daytime, but this is not common due to problems with the storage space. INDUSTRIAL APPLICABILITY The present invention can produce an energy carrier that can be moved, has a small volume, and can be easily stored with a small amount of electric power, and can provide it as power generation energy at any place regardless of daytime and nighttime.
【0005】[発明の実施の形態]本発明の実施例を図
面に従って説明すれば次のようである。図の1は公知の
液化炭酸ガス製造機とドライアイス製造機コーナーでA
は原料ガスのタンク、Bはガスホルダー、Cは洗浄機、
Dは炭酸ガス圧縮機、Eは脱臭機、Fは脱湿機、Gは冷
凍機を併設した炭酸ガス液化機、Hは液化炭酸ガス貯蔵
タンク、Iはドライアイス製造装置、Jはドライアイス
プレス機、Kは固形化ドライアイス、図の2はドライア
イスの気化機と加圧炭酸ガスモーターと発電機のコーナ
ー。Lは寒剤を収納したドライアイス気化機、Nは調圧
弁付きの加圧炭酸ガス用のタンク。Oはガスタービン乃
至圧搾空気モーター類似の加圧ガスモーターによる発電
機、Pはガス回収タンク。Mはガス乃至不凍液を媒体と
する過冷却防止機BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. Figure 1 is the corner of the known liquefied carbon dioxide production machine and dry ice production machine.
Is a source gas tank, B is a gas holder, C is a washing machine,
D is a carbon dioxide compressor, E is a deodorizer, F is a dehumidifier, G is a carbon dioxide liquefier with a refrigerator, H is a liquefied carbon dioxide storage tank, I is a dry ice production device, and J is a dry ice press. Machine, K is solidified dry ice, 2 in the figure is a dry ice vaporizer, pressurized carbon dioxide motor and generator. L is a dry ice vaporizer containing a cryogen, and N is a tank for pressurized carbon dioxide with a pressure regulator. O is a generator using a pressurized gas motor similar to a gas turbine or a compressed air motor, and P is a gas recovery tank. M is a supercooling prevention device that uses gas or antifreeze as a medium
【0006】[実施例]深夜乃至余剰電力を用い二酸化
炭素を公知の液化炭酸ガス製造機図1のC〜Hで加圧冷
却し液化した後、I〜Jのドライアイス製造機中に噴出
させドライアイスに変換し固形化したものをエネルギー
担体とし、必要に応じ図2のLのアルコール、アセトン
等の寒剤中で突沸的に昇華させ、加圧ガスを作り図2の
Nのガスタンクを経て調圧し、図2のOのガスタービン
乃至ロータリーベーン型、ラジアルピストン型等の圧搾
空気モーター類似のガスモーターの回転エネルギーを発
電エネルギーに変換したるを特徴とする二酸化炭素のエ
ネルギー担体化とその利用法である。この排出ガスは回
収し、寒剤のタンクのLの低温を過冷却防止機Mを利用
し、図1のGの冷凍機に還流し液化炭酸がスの冷却の補
助としての使用も可能である。[Example] Carbon dioxide was liquefied by pressure cooling at a known liquefied carbon dioxide production machine C-H in the known liquefied carbon dioxide production machine from midnight to surplus power, and then jetted into the dry ice production machines I to J. The solidified product converted to dry ice is used as an energy carrier, and if necessary, it is sublimated in a freezing agent such as alcohol or acetone of L in FIG. 2 to make a pressurized gas, and the gas is adjusted through the N gas tank of FIG. The energy carrier of carbon dioxide, which is characterized by converting the rotational energy of a gas motor similar to a compressed air motor such as a gas turbine of O of FIG. 2 or a rotary vane type or a radial piston type of FIG. Is. This exhaust gas can be recovered and the low temperature of L in the cryogen tank can be returned to the refrigerator of G of FIG.
図の1は液化炭酸ガス製造機とドライアイス製造機の側
面図。図の2はドライアイス気化機と加圧炭酸ガスのタ
ンクと圧縮ガスによる発電機の側面図Figure 1 is a side view of a liquefied carbon dioxide production machine and a dry ice production machine. Figure 2 is a side view of the dry ice vaporizer, pressurized carbon dioxide gas tank, and generator using compressed gas.
Aは原料ガスのタンク、Bはガスホルダー、Cは洗浄
機、Dは炭酸ガス圧縮機、Eは脱臭機、Fは脱湿機、G
は冷凍機を併設した炭酸ガス液化機Hは液化炭酸ガス貯
蔵タンク、Iはドライアイス製造装置、Jはドライアイ
スプレス機、Kは固形化ドライアイス、Lはドライアイ
スの気化機、Nは調圧弁付きの加圧炭酸ガス用のタン
ク、Oはガスタービン乃至圧搾空気モーター類似の加圧
ガスモーターによる発電機、Pはガス回収タンクMはガ
ス乃至不凍液を媒体とする過冷却防止機。A is a raw material gas tank, B is a gas holder, C is a washing machine, D is a carbon dioxide gas compressor, E is a deodorizer, F is a dehumidifier, and G is a dehumidifier.
Is a liquefied carbon dioxide gas liquefier equipped with a refrigerator H is a liquefied carbon dioxide gas storage tank, I is a dry ice production device, J is a dry ice press machine, K is solidified dry ice, L is a dry ice vaporizer, and N is a control device. A tank for pressurized carbon dioxide gas with a pressure valve, O is a generator using a gas turbine or a pressurized gas motor similar to a compressed air motor, P is a gas recovery tank M is a supercooling prevention device using gas or antifreeze as a medium.
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成14年1月7日(2002.1.7)[Submission date] January 7, 2002 (2002.1.7)
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】図面の簡単な説明[Name of item to be corrected] Brief description of the drawing
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図面の簡単な説明】[Brief description of drawings]
【図1】図の1は液化炭酸ガス製造機とドライアイス製
造機の側面図FIG. 1 is a side view of a liquefied carbon dioxide production machine and a dry ice production machine.
【図2】図の2はドライアイス気化機と加圧炭酸ガスの
タンクと圧縮ガスによる発電機の側面図FIG. 2 is a side view of a dry ice vaporizer, a pressurized carbon dioxide gas tank, and a compressed gas generator.
【符号の説明】
Aは原料ガスのタンク、Bはガスホルダー、Cは洗浄
機、Dは炭酸ガス圧縮機、Eは脱臭機、Fは脱湿機、G
は冷凍機を併設した炭酸ガス液化機 Hは液化炭酸ガス
貯蔵タンク、Iはドライアイス製造装置、Jはドライア
イスプレス機、Kは固形化ドライアイス、Lはドライア
イスの気化機、Nは調圧弁付きの加圧炭酸ガス用のタン
ク、Oはガスタービン乃至圧搾空気モーター類似の加圧
ガスモーターによる発電機、Pはガス回収タンク Mは
ガス乃至不凍液を媒体とする過冷却防止機。[Explanation of Codes] A is a tank for raw material gas, B is a gas holder, C is a washing machine, D is a carbon dioxide gas compressor, E is a deodorizer, F is a dehumidifier, and G is a dehumidifier.
Is a liquefied carbon dioxide liquefier equipped with a refrigerator. H is a liquefied carbon dioxide storage tank, I is a dry ice production device, J is a dry ice press machine, K is solidified dry ice, L is a dry ice vaporizer, and N is a controller. A tank for pressurized carbon dioxide with a pressure valve, O is a generator with a pressurized gas motor similar to a gas turbine or a compressed air motor, P is a gas recovery tank, and M is a supercooling prevention device using gas or antifreeze as a medium.
【手続補正2】[Procedure Amendment 2]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】全図[Correction target item name] All drawings
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図1】 [Figure 1]
【図2】 [Fig. 2]
Claims (3)
加圧冷却し液化した後、ドライアイスに変換し固形化し
たものをエネルギー担体とし、1. Carbon dioxide is pressurized and cooled from midnight to surplus power to be liquefied, and then converted to dry ice and solidified to obtain an energy carrier,
寒剤中で、突沸的に昇華させ、加圧ガスを作り、ガスタ
ンクを経て調圧し2. If necessary, in a cryogen such as alcohol or acetone, it is sublimated by bumping to make a pressurized gas, and the pressure is adjusted via a gas tank.
至圧搾空気モーター類似のガスモーターの回転エネルギ
ーを発電エネルギーに変換したるを特徴とする二酸化炭
素のエネルギー担体化とその利用法である。3. A method of using carbon dioxide as an energy carrier, characterized in that the rotational energy of a gas turbine or a gas motor similar to a compressed air motor is converted into power generation energy by the pressurized gas fed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001363459A JP2003126681A (en) | 2001-10-24 | 2001-10-24 | Carbon dioxide as energy carrier and use of the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001363459A JP2003126681A (en) | 2001-10-24 | 2001-10-24 | Carbon dioxide as energy carrier and use of the same |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003126681A true JP2003126681A (en) | 2003-05-07 |
Family
ID=19173794
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001363459A Pending JP2003126681A (en) | 2001-10-24 | 2001-10-24 | Carbon dioxide as energy carrier and use of the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003126681A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011505537A (en) * | 2007-11-26 | 2011-02-24 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | Adaptation of oxy-combustion plants to energy utilization and the amount of CO2 to be captured |
CN102767428A (en) * | 2012-08-15 | 2012-11-07 | 李伟 | Heat absorption type dry ice engine |
JP2016196860A (en) * | 2015-04-06 | 2016-11-24 | 健児 廣瀬 | Power generation device |
GB2559019A (en) * | 2016-12-01 | 2018-07-25 | Ccm Res Limited | Power generation |
GB2565811A (en) * | 2017-08-23 | 2019-02-27 | Engen House F Z C | Sublimal sequential condensation carbon dioxide turbine (SSCCDT) |
WO2020147918A1 (en) | 2019-01-14 | 2020-07-23 | Engen House F.Z.C | Turbine system |
EP4056815A1 (en) * | 2021-03-12 | 2022-09-14 | Hamilton Sundstrand Corporation | Carbon dioxide sublimation generator |
-
2001
- 2001-10-24 JP JP2001363459A patent/JP2003126681A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011505537A (en) * | 2007-11-26 | 2011-02-24 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | Adaptation of oxy-combustion plants to energy utilization and the amount of CO2 to be captured |
CN102767428A (en) * | 2012-08-15 | 2012-11-07 | 李伟 | Heat absorption type dry ice engine |
JP2016196860A (en) * | 2015-04-06 | 2016-11-24 | 健児 廣瀬 | Power generation device |
GB2559019A (en) * | 2016-12-01 | 2018-07-25 | Ccm Res Limited | Power generation |
GB2559019B (en) * | 2016-12-01 | 2019-06-26 | Ccm Res Limited | Power generation |
US10895173B2 (en) | 2016-12-01 | 2021-01-19 | CCm Technologies Limited | Power generation |
GB2565811A (en) * | 2017-08-23 | 2019-02-27 | Engen House F Z C | Sublimal sequential condensation carbon dioxide turbine (SSCCDT) |
WO2020147918A1 (en) | 2019-01-14 | 2020-07-23 | Engen House F.Z.C | Turbine system |
EP4056815A1 (en) * | 2021-03-12 | 2022-09-14 | Hamilton Sundstrand Corporation | Carbon dioxide sublimation generator |
US11454138B1 (en) | 2021-03-12 | 2022-09-27 | Hamilton Sundstrand Corporation | Carbon dioxide sublimation generator |
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