TWI298782B - Energy circulation system and method thereof - Google Patents

Energy circulation system and method thereof Download PDF

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Publication number
TWI298782B
TWI298782B TW95109397A TW95109397A TWI298782B TW I298782 B TWI298782 B TW I298782B TW 95109397 A TW95109397 A TW 95109397A TW 95109397 A TW95109397 A TW 95109397A TW I298782 B TWI298782 B TW I298782B
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Taiwan
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energy
gas
heat
brine
heat exchange
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TW95109397A
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Chinese (zh)
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TW200741148A (en
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Hsin Chi Su
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Tawwan Maritime Transp Co Ltd
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Description

1298782 aforesaid devices. A cold energy generated by the gas by vaporizing the liquid and a heat energy generated by blazing the gas are used to achieve various energy applications. 七、指定代表圖: (一) 本案指定代表圖為:第(二)圖。 (二) 本代表圖之元件符號簡單說明: 21 :熱交換裝置; 22 :室内循環機制;以及 211 :氣體; 221 :鹵水。 212 : _水; 八、 本案右有化學式時,請揭示最能顯示發明特徵的化學式: 九、 發明說明: # 【發明所屬之技術領域】 ‘ 明係為—種能源彳盾縣統及其方法,特别是關於利 ,% =田天然氣汽化過程的熱交換及體積變化,達成能源的 樵k刺用。 【先前技術】 物二Γ二為化石燃料中較為潔淨之能源,燃燒時無硫氧化 物ω〇產生,而產生之氮氧化 之 〜4〇%’二氣化碳⑽)為煤炭之_,是各國改善空氣 41298782 aforesaid devices. A cold energy generated by the gas by vaporizing the liquid and a heat energy generated by blazing the gas are used to achieve various energy applications. VII. Designated representative map: (1) The representative representative of the case is: ) Figure. (ii) A brief description of the symbol of the representative figure: 21: heat exchange device; 22: indoor circulation mechanism; and 211: gas; 221: brine. 212 : _ water; VIII. When there is a chemical formula on the right, please disclose the chemical formula that best shows the characteristics of the invention: IX. Description of the invention: # [Technical field to which the invention belongs] 'Ming system is a kind of energy 彳 shield county system and its method In particular, regarding the profit, % = heat exchange and volume change of the natural gas vaporization process, to achieve the energy of the thorns. [Prior Art] Titanium II is a relatively clean energy source in fossil fuels. When it is burned, no sulfur oxides, ω〇, are produced, and the nitrogen oxides produced by ~4〇% 'dicarbonized carbon (10)) are coal. Countries improve air 4

1298782 污染及減少二氧化碳相當好的能源選項,加上天然氣可協助 ,國達到能源多元化目標以減少對進口石油的依賴,故天然 氣的多元應用是一重要的課題。 目前,天然氣的運用多使用汽化後的天然氣,請參閱第 一圖’係為習知天然氣的運輸到使用的過程示意圖。圖中, 天然氣由產地產出並加以液化後,裝置於液化天然氣運輸船 U,運至目的地卸下儲存於冷凍儲槽12中,接著經由汽化 過程13將液態的天然氣還原為氣態的天然氣後,以 送至使用端14使用。 然而,一般大眾所利用到的是已汽化後的天然氣,無形 就浪費了液化天然氣汽化過程中的冷凍效果。為滿足所提 欠的夕元利用的需求’本發明人基於多年從事研究與諸多實 t驗L經多方研究設計與專題探討,遂於本發明提出-種 犯6、循㈣統及其方法以作為前述期望—實現方式與依據。 【發明内容】 W Ϊΐ於上述課題,本發明之目的為提供—雖源循料 =其方法,特別是關於利用將液化 = 換及體積變化,達成能源的循環_。 4的熱父 、^是,根據本發明的目的,提出一種能源循環 二熱交換裝置及室内循環機制。其中,熱交換事: 出以將—液體汽化成-氣體,其後,ί :體及失去熱1之豳水,室内循 ^輸 错由循環鹵水提供至少-n w 又換裝置, 之氣體予至少-燃燒裝置產生升及供給上述 之南水循環回熱交換裝置;_ 4新吸收熱量 液體汽化a裔舻所吝、人構成一此源循環系統,盖用 〜化—植生之冷能及 。用 5 1298782 根據本發明的目的,另可於能源 裝置,其藉由氣體驅動渦輪裝置產生一 “=、、先中増加一渦輪 置、燃燒裝置或一電器裝置所需之2電能,以供給降溫裝 液化裝置利用電能或失去熱量 ^時’更可增加- 成液體。 將°卩份氣體重新液化 緣是’根據本發明之目的,提出 步驟包含有藉由一熱交換裝置傳導—广原循環方法,其 液體汽化成-氣體,其後,輸出氣體及熱量以將-及,提供一建物並於豆内逢罟一〜大专熱I之鹵水;以 裝置,藉循環鹵水提供至少—降^ 連接熱交換 水循環回熱交換裝置。 並將重新吸收熱量之鹵 前述液體及氣體之及其方法,善用 的。 連成多兀應用能源的目 功效=委員對本發明之技術特徵及所達成之 ;關圖式以為辅佐之用,並以詳細之說明二 【實施方式】 ^㈣相關圖式,朗依本發明較佳實施例之能源 ^糸統及其方法,為使便於理解’其中相同的元件將以相 同的元件符號加以說明。 請參閱第二圖,係顯示本發明之一能源循環系統之示意 二°圖中,能源循環系統包含有_熱交換裝置21及一室内 循環機制22。其中’熱交換裝置21用於傳導_水之熱量以 6 1298782 將液體汽化成氣體,其後,輸出氣體211及失去熱量之鹵水 212,至内循%機制2 2連接熱交換裳置21,藉由循壞鹵水 212提供至少一降溫裝置之降溫功能 211予至少 ; X ^ 221 循環回熱父換裝置21。另外,熱交換裝置2ι更包含有一製 ^迴路及一汽化迴路,製冷迴路用於循環鹵水以傳導熱量, 汽化迴路使液體吸收熱量以汽化為氣體,且製冷迴路更連結 至少一泵浦用以循環鹵水。 一請參閱第三圖,係顯示本發明之一較佳實施例之能源循 2統圖、。圖中’能源循環系統由熱交換裝置31自 #提供液化天然氣’以傳導齒水之熱量將液化天然 1天/1氣’並輪出天然氣312及失去熱量之4水 313提二機制32連接熱交換褒置31,藉由循環1^水 及提降溫裝置之降溫功能 循環回熱交換敦m中且教=新4收二量之由水奶 存槽化天然氣以提更可产含-儲 意圖。能源猶料^人不女本發明之另一能源骑m系統之示 41' 成氣體411,漏輪裝 熱父換裝置41將液體汽化 生一電能421,並藉此雷=^體411驅動洞輪裂置42產 液體之用,另,室 421以作為熱交換较置41汽化 輪裝置42,以供仏* =機制43更連接熱交換骏置41及$ 此》η丨X币仏、七乳體411予至少一辦士置41及屑 此及引入魏421 μ恤㈣生升溫功 7 1298782 口月參閱第五圖,係顯示本發 循環系統之示意圖。圖中, 較佳實施例之能源 將液化天然氣汽化成天然氣5ΐΓ·、1^統由熱交換裝置51 511驅動渦輪引擎52產生輪弓丨擎52藉由天然氣 為熱交換裳置51汽化液化天然^ 21 田並藉此電能521以作 53更連接熱交換裝置51及渦 ,3,室内循環機制 予如瓦斯壚、室内空調、暖氣機或供給天然氣⑴ 溫功能及引入521彳i^、、、水态之燃燒裝置產生升 ^ 作為各式電器裝置或降溫之用。1298782 Pollution and carbon dioxide are quite good energy options, plus natural gas can help, the country achieves energy diversification goals to reduce dependence on imported oil, so the multi-application of natural gas is an important issue. At present, the use of natural gas uses more natural gas after vaporization. Please refer to the first figure for a schematic diagram of the process of transporting and using natural gas. In the figure, after the natural gas is produced and liquefied by the production area, it is installed on the LNG carrier U, transported to the destination for unloading and stored in the freezing storage tank 12, and then the liquid natural gas is reduced to gaseous natural gas via the vaporization process 13. , to be sent to the use terminal 14 for use. However, the general public has used the vaporized natural gas, which invisibly wastes the freezing effect during the vaporization of the liquefied natural gas. In order to meet the demand of the yawning utilization of the owed by the inventor, the inventor based on many years of research and many real t-tests through multi-party research design and special discussion, 遂 本 本 种 种 种 种 种 种 、 、 、 、 、 、 、 、 、 、 As the aforementioned expectations - implementation and basis. SUMMARY OF THE INVENTION In order to solve the above problems, it is an object of the present invention to provide a method for the production of energy, in particular, for the use of liquefaction = volume change to achieve energy cycle _. The hot father of 4, in accordance with the purpose of the present invention, proposes an energy cycle two heat exchange device and an indoor circulation mechanism. Among them, the heat exchange thing: the vaporization of the liquid into a gas, and then, ί: body and the loss of heat 1 of the water, the indoor error is provided by the circulating brine to provide at least -nw and the device, the gas to at least - The combustion device generates and supplies the above-mentioned south water circulation to the heat exchange device; _ 4 newly absorbed heat liquid vaporizes a 舻 舻 吝 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人 人5 1298782 According to the object of the present invention, another energy device can be used to generate a "=, first medium, plus a turbine, a combustion device or an electrical device to supply a cooling device by means of a gas-driven turbine device. When the liquefaction device utilizes electric energy or loses heat, it can be increased to become a liquid. Re-liquefaction of the gas is "for the purpose of the present invention, the proposed step includes conduction by a heat exchange device - Guangyuan cycle method The liquid is vaporized into a gas, and thereafter, the gas and heat are output to provide a structure and a brine in the bean, and the brine is provided in the bean; Exchanging water circulation back to the heat exchange device. It will re-absorb the heat and the above-mentioned liquid and gas and its method. It will be used in conjunction with the energy efficiency of the application of the energy = the technical characteristics and achievements of the present invention; The formula is used as an aid, and in detail, the second embodiment [embodiment] ^ (four) related diagram, the energy system and method thereof according to the preferred embodiment of the present invention, for the convenience The same elements will be described with the same element symbols. Please refer to the second figure, which shows a schematic diagram of an energy circulation system of the present invention, the energy circulation system includes a heat exchange device 21 and an indoor Circulation mechanism 22. Among them, the heat exchange device 21 is used for conducting heat of water to vaporize the liquid into gas at 6 1298782, and thereafter, the gas 211 and the brine 212 which loses heat are transferred to the internal mechanism 2 2 to connect the heat exchange skirt. 21, the cooling function 212 of the at least one cooling device is provided by the circulating brine 212 to at least; X^221 is recycled to the hot parent device 21. In addition, the heat exchange device 2i further comprises a circuit and a vaporization circuit for cooling The circuit is used to circulate brine to conduct heat, the vaporization circuit causes the liquid to absorb heat to vaporize into a gas, and the refrigeration circuit is further coupled with at least one pump for circulating brine. Referring to the third figure, a preferred embodiment of the present invention is shown. For example, the energy source follows the 2 diagram. In the figure, the 'energy circulation system is supplied by the heat exchange unit 31 from #liquefied natural gas' to conduct the heat of the tooth water to liquefy the natural one day / 1 gas. 'And take out the natural gas 312 and lose heat 4 water 313 to mention the second mechanism 32 to connect the heat exchange device 31, by circulating 1 ^ water and cooling device cooling function to cycle back to heat exchange and teach = new 4 The second quantity is made up of water milk to store natural gas to improve the production-containing storage intention. The energy is still expected to be non-female, the other energy of the invention, the m-system display 41' into the gas 411, the leaky wheel is replaced by the hot father The device (41) vaporizes the liquid to generate a power 421, and thereby the worm body 411 drives the wormhole 42 to produce a liquid. Further, the chamber 421 serves as a heat exchange unit 41 for the smelting wheel device 42 for 仏* = Mechanism 43 is more connected to the heat exchange Jun 41 and $ 丨 丨 X coins, seven breasts 411 to at least one clerk set 41 and the same and introduced Wei 421 t shirt (four) heat heating work 7 1298782 The figure shows a schematic diagram of the present cycle system. In the figure, the energy of the preferred embodiment vaporizes the liquefied natural gas into natural gas. The heat exchanger unit 51 511 drives the turbine engine 52 to produce the wheel bow engine 52. The natural gas is heat exchanged and the gas is vaporized and liquefied. 21 Tian and the electric energy 521 for 53 more connected heat exchange device 51 and vortex, 3, indoor circulation mechanism to such as gas, indoor air conditioning, heating or supplying natural gas (1) temperature function and introduction of 521彳i^,,, water state The combustion device generates the riser ^ as a variety of electrical devices or for cooling.

明翏閱第六圖,係顯示本發明直^降咖衣置之用。 意圖。能—環祕包含有再—錢循環系統之示 62、一液化聲w 芬一^如/、、、又換凌置61、一渦輪裝置 W R1 ffl 至内循環機制64。其中,埶交換裝 置61用於傳導i水之熱量以將液體 :j換f 出氣體611及失去埶詈之内匕 /成軋體,其後,輸 齒水渦輪裝置62藉由氣體 產生一電能621’液化裝置63利用電能奶 2將部份氣體611重新液化成液體,室 制64連接熱交換裝置6卜藉由循環齒水612提供 ^^一降溫裝置之降溫功能及供給氣體611予至少一燃燒 裝置產^升溫功能,並將重新吸收熱量之_水631及641 自液化裝置63及室内循環機制64循環回熱交換裝置61。 另外,熱交換裝置61更包含有一製冷迴路及一汽化迴路, 製冷迴路用於循環齒水以傳導熱量,汽化迴路使液體吸收熱 量以汽化為氣體,且製冷迴路更連結至少一泵浦用以循環鹵 水0 請參閱第七圖,係顯示本發明之再一較佳實施例之能源 循環系統之示意圖。圖中,能源循環系統由熱交換裝置71 用於傳導i水之熱量以將液化天然氣汽化成天然氣,其後, 輸出天然氣711及失去熱量之鹵水712,渦輪引擎72藉由 8The sixth figure shows the use of the present invention. intention. The energy-ring secret contains the re-currency system. 62, a liquefied sound w, a fen-like, such as /,, and then a transformer 61, a turbine device W R1 ffl to the inner circulation mechanism 64. Wherein, the helium exchange device 61 is configured to conduct heat of the i water to exchange the liquid: j for the gas 611 and the inner crucible/formed rolling body, and thereafter, the water turbine device 62 generates an electric energy by the gas. The 621' liquefaction device 63 re-liquefies the partial gas 611 into a liquid by using the electric energy milk 2, and the chamber 64 connects the heat exchange device 6 to provide a cooling function of the cooling device and the supply gas 611 to at least one by the circulating tooth water 612. The combustion device generates a heating function, and the heat-removing water 631 and 641 are recycled from the liquefaction device 63 and the indoor circulation mechanism 64 to the heat exchange device 61. In addition, the heat exchange device 61 further includes a refrigeration circuit for circulating the tooth water to conduct heat, the vaporization circuit for absorbing heat to vaporize the gas, and the refrigeration circuit is further coupled with at least one pump for circulation. Brine 0 Referring to the seventh drawing, there is shown a schematic diagram of an energy circulation system according to still another preferred embodiment of the present invention. In the figure, the energy circulation system is used by the heat exchange device 71 to conduct heat of the i water to vaporize the liquefied natural gas into natural gas, and thereafter, the natural gas 711 and the heat-removed brine 712 are output, and the turbine engine 72 is provided by 8

1298782 電d t 曰產生一電能721 ’液化裝置73利用 ί ΐ或熱置之齒水712將部份天然氣711重新丄μ 成液體’/_環_ 74連接熱交換裝置7卜藉由循^匕 水712提供如室内空調、冷氣機或冰箱之降溫裝置之降温功 能及供給天然氣711予如瓦斯爐、室内空調、暖氣機或 器之燃燒裝置產生升溫功能,並將重新吸收熱量之_水、7^ 及741自渦輪引擎72及室内循環機制74循環回熱交換裝置 71。 請參閱第八圖,係顯示本發明之熱交換裝置之示意圖。 圖中,熱父換I置81包含有一製冷迴路82及一汽化趣路 83。其中,製冷迴路82具有至少一第一入口 821以供給— 鹵水及至少一第一出口 822以排出鹵水,而鹵水則藉由該製 冷迴路82傳導一熱量84,汽化迴路⑽具有i少一第二入 口 831以供給〆液體及至少一第二出口 832以排出—氣體, 真液醴藉由汽化迴路83吸收熱量84以汽化為氣體。另外, 製冷迴路更連詰至少一泵浦用以循環鹵水。 ^第九圖係顯示本發明之一較佳實施例之熱交換裝置之 济意圖。第十圖係顯示本發明之一較佳實施例之熱交換裝置 及儲存槽之示意圖。第十一圖係顯示本發明之另一較佳實施 例之熱交換裝置結合儲存槽之示意圖。 請一併參閱弟九圖、弟十圖及第十一圖。如弟九圖所示 之熱交換裝置91具有一汽化迴路之第二入口 92以供給液化 天然氣於吸收熱里後由弟一出口 93排出天然氣,且亦包含 有〆製冷迴路94其自第一入口 941供給鹵水,鹵水則藉由 製冷迴路94傳導熱1後由第一出口 942排出。如第十圖所 米將熱交換裝置91之第一入口 92連接於一儲存槽al,由 儲存槽al 一入口 a11存入液化天然氣,且由一出口 al2供 9 1298782 給液化天然氣至第二入口 ” 換H Μ h9 ^又,如第十一圖所示之熱交 在入H二 於一體,儲存槽b2由一入口 b21 換裝置Μ之多個第二入:出二22供給液化天然氣至熱交 中的製冷迴路的齒水由第_^圖中未標示),熱交換裝置bl :12。排出,將液化天•心天: = 化成Ϊ^11:#Ι由熱交換裝置傳導鹵水之熱量以將液體汽 ,S12 1出氣體及失去熱量之齒水; 以及 ’驟S13 ·提供-建物並於其内建置—室内循環機制; 水接二^幻4 ·將室内循環機制連接熱交換裝置,藉循環鹵 燒麥署、客^ 一降溫裝置之降溫功能及供給氣體予至少一燃 置。生升溫功能,並將重新吸收熱量之鹵水循環回熱交 體之動更可提供一渦輪裝置於此方法中,渦輪裝置藉由氣 置所二^生一電能,以供給降溫裝置、燃燒裝置或電器裝 之鹵二之電力,且更可提供一液化裝置利用電能或失去熱量 輪^丨^,將部份氣體重新液化成液體。渦輪裝置一般可為渦 製A、回’而熱交換裝置更包含有一製冷迴路及一汽化迴路, ί二,路用於循環_水以傳導熱量,汽化迴路使液體吸收熱 水,化為氣體,且製冷迴路更連結至少一泵浦用以循環鹵 時,’、可包含一儲存槽以儲存液體以提供作為汽化之用。同 τ此方法中之液體係為液化天然氣,氣體係為天然氣,降 1298782 溫裝置可為室内空調、冷氣機或冰箱等,燃燒裝置可為瓦斯 爐、室内空調、暖氣機或熱水器等。 綜上所述,本發明各施實例中係利用_水以應用液化天 然氣之冷能’而此齒水需具備比熱大、熱傳導係數高、凍結 點低、無燃燒性、無毒性、無***性及對金屬管之腐蝕性小 的條件,方為理想之鹵水。其中,凍結點是一相當重要的條 件’若凍結點不夠低,將造成_水凍結無法循環傳遞冷能, 因此,凍結點係指液體中之水份開始結冰之溫度。通常清水 在〇°c時開始凍結,而溶有溶質之溶液之凍結點較〇沱略 低,束結點降低之程度是隨著溶劑之種類和溶質之浪度而有 5 ί Ϊ ,均是隨溶f濃度愈高則;東結點愈下降。現今所使 用的齒水種類,各有其優缺點;例如 液,腐蝕性強,管線需要傕用射虛盈从柘低廉的虱化鈣洛 的甲醇系溶液,使用時需考,、安全=料;具有引火性 醇及丙稀乙二醇兩者點度高:在應匕=對策;乙婦乙二 增加搬送動力及使機器尺寸加大的 二限制,通常會有 不之各種鹵水之特性表,龙思,靖翏閱第十三圖所 乙二醇、丙二醇等水、氯倾、酒精、 ’其均為藉由液體 ;j符合需求之鹵水溶 _態’始終保持液態的冷===象吸熱,為—種不改 以上所述僅為舉例性,而,媒介物。 發明之精神與|| _ 為限制性者 冬對其進行之耸兮# 任何未脫離本 3於後附之申請專利籁ιΐί + 等攻修改或變更,均應包 1298782 【圖式簡單說明】 第一圖係為習知天然氣的運輸到使用的過程示意圖; 第二圖係顯示本發明之一能源循環系統之示意圖; 第三圖係顯示本發明之一較佳實施例之能源循環系統之 不意圖, 第四圖係顯示本發明之另一能源循環系統之示意圖; 第五圖係顯示本發明之另一較佳實施例之能源循環系統 之不意圖, 第六圖係顯示本發明之再一能源循環系統之示意圖; 第七圖係顯示本發明之再一較佳實施例之能源循環系統 之不意圖, 第八圖係顯示本發明之熱交換裝置之示意圖; 第九圖係顯示本發明之一較佳實施例之熱交換裝置之示 意圖, 第十圖係顯示本發明之一較佳實施例之熱交換裝置及儲 存槽之示意圖; 第十一圖係顯示本發明之另一較佳實施例之熱交換裝置 結合儲存槽之示意圖; 第十二圖係為本發明之能源循環方法之流程圖;以及 第十三圖係顯示各種鹵水溶液之特性表。 12 1298782 【主要元件符號說明】 11 :液化天然氣運輸船; 12 :冷珠儲槽; 13 :汽化過程; 14 :使用端; 21、 31、41、51、61、71、81、91 及 bl :熱交換裝置; 211、 311·及 611 :氣體; 212、 22卜 313、32卜 612、63卜 64卜 712、731 及 741 ··鹵水; 22、 43、53、64及74 :室内循環機制; 31 卜 a21 及 bll :入口; 312、511及711 :天然氣; 42及62 :渦輪裝置; 42卜 521、621 及 721 :電能; 52及72 :渦輪引擎; 63及73 :液化裝置; 82及94 :製冷迴路; 821、 941 及 bll :第一入口; 822、 942 及 bl2 :第一出口; 83 :汽化迴路; 831及92 :第二入口; 832、93 及 bl3 :第二出口; 84 :熱量; al及b2 :儲存槽; al2及b22 :出口;以及 S11〜S14 :流程步驟。 131298782 Electric dt 曰 generates an electric energy 721 'The liquefaction device 73 re-pulsing part of the natural gas 711 into liquid '/_ ring _ 74 using the tooth water 712 or the hot tooth 712 to connect the heat exchange device 7 712 provides cooling function such as indoor air conditioner, air conditioner or refrigerator cooling device and supplies natural gas 711 to the combustion device such as gas stove, indoor air conditioner, heater or device to generate heating function, and will re-absorb heat _ water, 7^ The 741 is circulated back to the heat exchange unit 71 from the turbine engine 72 and the indoor circulation mechanism 74. Referring to the eighth drawing, there is shown a schematic view of the heat exchange apparatus of the present invention. In the figure, the hot parent switch I 81 includes a refrigeration circuit 82 and a vaporization circuit 83. The refrigeration circuit 82 has at least one first inlet 821 for supplying brine and at least one first outlet 822 for discharging brine, and the brine is conducted by the refrigeration circuit 82 to conduct a heat 84, and the vaporization circuit (10) has a second and a second. The inlet 831 supplies the helium liquid and the at least one second outlet 832 to discharge the gas, and the liquid helium absorbs the heat 84 by the vaporization circuit 83 to be vaporized into a gas. In addition, the refrigeration circuit is connected to at least one pump for circulating brine. The ninth drawing shows the intention of the heat exchange apparatus of a preferred embodiment of the present invention. Figure 11 is a schematic view showing a heat exchange device and a storage tank in accordance with a preferred embodiment of the present invention. Fig. 11 is a view showing a heat exchange device in combination with a storage tank according to another preferred embodiment of the present invention. Please also refer to the brother Jiu Tu, the 10th and 11th. The heat exchange device 91 shown in FIG. 9 has a second inlet 92 of a vaporization circuit for supplying liquefied natural gas to absorb heat, and the natural gas is discharged from the first outlet 93, and also includes a helium refrigeration circuit 94 from the first inlet. The 941 is supplied with brine, which is discharged by the first outlet 942 after the heat is conducted by the refrigeration circuit 94. As shown in the tenth figure, the first inlet 92 of the heat exchange device 91 is connected to a storage tank a1, the storage tank a1 is stored in the liquefied natural gas, and the outlet a1 is supplied to the liquefied natural gas to the second inlet.换H Μ h9 ^ Again, as shown in Figure 11, the heat is placed in H, the storage tank b2 is replaced by an inlet b21, and the second inlet: the second 22 is supplied to the liquefied natural gas to the heat. The tooth water of the refrigerating circuit in the intersection is not marked by the _^ diagram, and the heat exchange device bl:12. Discharge, liquefy the sky • Xintian: = into Ϊ^11: #ΙThe heat of the brine is conducted by the heat exchange device To send liquid steam, S12 1 out of gas and tooth water that loses heat; and 'S13 · Provide - construction and build it inside - Indoor circulation mechanism; Water connection 2 ^ Magic 4 · Connect indoor circulation mechanism to heat exchange device By means of the circulating halogen-burning mill, the cooling function of the cooling device and the supply of gas to at least one of the burners, the heating function and the re-absorption of the brine to the heat exchanger can provide a turbine device. In this method, the turbine device is produced by the gas device. The electric energy is used to supply the power of the cooling device, the burning device or the electric device, and further provides a liquefaction device to re-liquefy part of the gas into a liquid by using electric energy or losing heat. The turbine device is generally vortex. The system A and the heat exchanger further comprise a refrigeration circuit and a vaporization circuit, and the circuit is used for circulating water to conduct heat, and the vaporization circuit allows the liquid to absorb hot water and turn into gas, and the refrigeration circuit is further connected to at least When a pump is used to circulate halogen, ', a storage tank may be included to store the liquid to provide vaporization. The liquid system in the method is liquefied natural gas, and the gas system is natural gas, and the temperature is reduced to 1287782. The air conditioner, the air conditioner or the refrigerator, etc., the combustion device may be a gas stove, an indoor air conditioner, a heater or a water heater, etc. In summary, in each of the examples of the present invention, the water is used to apply the cold energy of the liquefied natural gas. The water needs to have the conditions of larger heat, higher heat transfer coefficient, lower freezing point, no combustion, no toxicity, no explosion and less corrosiveness to the metal pipe. Among them, the freezing point is a very important condition. 'If the freezing point is not low enough, it will cause the water to freeze and cannot pass the cold energy. Therefore, the freezing point refers to the temperature at which the water in the liquid begins to freeze. Usually the water is in the water. The freezing point starts to decrease at °c, and the freezing point of the solution in which the solute is dissolved is slightly lower than that of the solute. The degree of the reduction of the beam point is 5 ί 随着 depending on the type of solvent and the solute of the solute. The higher the temperature, the lower the east node. The types of tooth water used today have their own advantages and disadvantages; for example, liquid, corrosive, and the pipeline needs to use a methanol solution of low-cost calcium sulphate , need to test when using, safety = material; with a high degree of ignition alcohol and propylene glycol: in the response = countermeasures; the second increase in the transmission power and the size of the machine, Usually there will be a variety of brine characteristics, Long Si, Jing Yu read the thirteenth figure of ethylene glycol, propylene glycol and other water, chlorine tilt, alcohol, 'all of them by liquid; j meet the needs of brine solution _ The state 'always keeps the liquid cold === like heat absorption, for the kind The above is only an example, but a medium. The spirit of the invention and || _ for the restrictive winter to carry it on the tower # Anyone who has not deviated from the application patent 籁ιΐί + etc. attached to this 3, etc., should be modified or changed, should be packaged 1287872 [Simple description of the diagram] 1 is a schematic diagram of a process of transporting and using natural gas; a second diagram showing a schematic diagram of an energy cycle system of the present invention; and a third diagram showing an intention of an energy cycle system according to a preferred embodiment of the present invention. The fourth figure shows a schematic diagram of another energy circulation system of the present invention; the fifth figure shows the intention of the energy circulation system of another preferred embodiment of the present invention, and the sixth figure shows another energy source of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 7 is a schematic view showing an energy circulation system according to still another preferred embodiment of the present invention, and FIG. 8 is a schematic view showing a heat exchange device of the present invention; BRIEF DESCRIPTION OF THE DRAWINGS FIG. 10 is a schematic view showing a heat exchange device and a storage tank according to a preferred embodiment of the present invention; and FIG. 11 is a view showing the present invention Another embodiment of the preferred embodiment the heat exchange means of binding a schematic view of the storage tank; circulation flow chart of a method of the present invention twelfth FIG energy system; and FIG thirteenth lines show the various characteristics of surface brine solution. 12 1298782 [Description of main components] 11: LNG carrier; 12: cold bead tank; 13: vaporization process; 14: use end; 21, 31, 41, 51, 61, 71, 81, 91 and bl: Heat exchange device; 211, 311, and 611: gas; 212, 22, 234, 32, 612, 63, 64, 712, 731, and 741 · brine; 22, 43, 53, 64, and 74: indoor circulation mechanism; 31 a21 and bll: inlets; 312, 511 and 711: natural gas; 42 and 62: turbines; 42 521, 621 and 721: electrical energy; 52 and 72: turbine engines; 63 and 73: liquefaction devices; : refrigeration circuit; 821, 941 and bll: first inlet; 822, 942 and bl2: first outlet; 83: vaporization circuit; 831 and 92: second inlet; 832, 93 and bl3: second outlet; ; al and b2: storage tank; al2 and b22: outlet; and S11~S14: process steps. 13

Claims (1)

1298782 十、申請專利範圍: 1、 一種能源循環系統,至少包含: 一熱交換裝置,用於傳導一鹵水之一熱量以將一液 體汽化成一氣體’其後9輸出該氣體及失去熱量之該 鹵水;以及 一室内循環機制,連接該熱交換裝置,藉由循環該 鹵水提供至少一降溫裝置之降溫功能及供給該氣體予 至少一燃燒裝置產生升溫功能,並將重新吸收熱量之 該鹵水循環回該熱交換裝置。 2、 如申請專利範圍第1項所述之能源循環系統,其中該 熱交換裝置更包含一製冷迴路及一汽化迴路,該製冷 迴路用於循環該鹵水以傳導該熱量,該汽化迴路使該 液體吸收該熱量以汽化為該氣體。 3、 如申請專利範圍第2項所述之能源循環系統,其中該 製冷迴路更連結至少一泵浦用以循環該鹵水。 4、 如申請專利範圍第1項所述之能源循環系統,其更包 含一渦輪裝置係藉由該氣體之驅動產生一電能,以供 給該降溫裝置、該燃燒裝置或一電器裝置所需之電力。 5、 如申請專利範圍第4項所述之能源循環系統,其中該 渦輪裝置係為一渦輪引擎。 6、 如申請專利範圍第4項所述之能源循環系統,其更包 含一液化裝置係利用該電能或失去熱量之該i水,將 部份該氣體重新液化成該液體。 7、 如申請專利範圍第1項所述之能源循環系統,其中該 液體係為一液化天然氣。 8、 如申請專利範圍第1項所述之能源循環系統,其中該 氣體係為一天然氣。 14 1298782 9、 如申請專利範圍第1項所述之能源循環系統,其中該 熱交換裝置更包含一儲存槽,係儲存該液體以提供作 為汽化之用。 10、 如申請專利範圍第1項所述之能源循環系統,其中 該降溫裝置係為一室内空調。 11、 如申請專利範圍第1項所述之能源循環系統,其中 該降溫裝置係為一冷氣機。 12、 如申請專利範圍第1項所述之能源循環系統,其中 該降溫裝置係為一冰箱。 13、 如申請專利範圍第1項所述之能源循環系統,其中 該燃燒裝置係為一瓦斯爐。 14、 如申請專利範圍第1項所述之能源循環系統,其中 該燃燒裝置係為一室内空調。 15、 如申請專利範圍第1項所述之能源循環系統,其中 該燃燒裝置係為一暖氣機。 16、 如申請專利範圍第1項所述之能源循環系統,其中 該燃燒裝置係為一熱水器。 17、 一種能源循環方法,至少包含: 藉由一熱交換裝置係傳導一鹵水之一熱量以將一液 體汽化成一氣體,其後,輸出該氣體及失去熱量之該 函水,以及 提供一建物並於其内建置一室内循環機制,連接該 熱交換裝置,藉循環該鹵水提供至少一降溫裝置之降 溫功能及供給該氣體予至少一燃燒裝置產生升溫功 能,並將重新吸收熱量之該鹵水循環回該熱交換裝置。 18、 如申請專利範圍第17項所述之能源循環方法,其更 包含提供一渦輪裝置係藉由該氣體之驅動產生一電 15 1298782 能,以供給該降溫裝置、該燃燒裝置或一電器裝置所 需之電力。 19、如申請專利範圍第18項所述之能源循環方法,其中 " 該渦輪裝置係為一渦輪引擎。 - 20、如申請專利範圍第18項所述之能源循環方法,其更 包含提供一液化裝置係利用該電能或失去熱量之該鹵 * 水,將部份該氣體重新液化成該液體。 . 21、如申請專利範圍第17項所述之能源循環方法,其中 該熱交換裝置更包含一製冷迴路及一汽化迴路,該製 • 冷迴路用於循環該鹵水以傳導該熱量,該汽化迴路使 該液體吸收該熱量以汽化為該氣體。 22、如申請專利範圍第21項所述之能源循環方法,其中 該製冷迴路更連結至少一泵浦用以循環該鹵水。 " 23、如申請專利範圍第17項所述之能源循環方法,其中 ' 該液體係為一液化天然氣。 24、 如申請專利範圍第17項所述之能源循環方法,其中 該氣體係為一天然氣。 25、 如申請專利範圍第17項所述之能源循環方法,其中 • 該熱交換裝置更包含一儲存槽,係儲存該液體以提供 , 作為汽化之用。 26、 如申請專利範圍第17項所述之能源循環方法,其中 看 該降溫裝置係為一室内空調。 27、 如申請專利範圍第17項所述之能源循環方法,其中 該降溫裝置係為一冷氣機。 28、 如申請專利範圍第17項所述之能源循環方法,其中 該降溫裝置係為一冰箱。 29、 如申請專利範圍第17項所述之能源循環方法,其中 16 1298782 該燃燒裝置係為一瓦斯爐。 30、 如申請專利範圍第17項所述之能源循環方法,其中 該燃燒裝置係為一室内空調。 31、 如申請專利範圍第17項所述之能源循環方法,其中 該燃燒裝置係為一暖氣機。 32、 如申請專利範圍第17項所述之能源循環方法,其中 該燃燒裝置係為一熱水器。1298782 X. Patent application scope: 1. An energy circulation system comprising at least: a heat exchange device for conducting heat of one of the brines to vaporize a liquid into a gas, and then outputting the gas and losing the heat of the brine And an indoor circulation mechanism connecting the heat exchange device, circulating the brine to provide a cooling function of the at least one cooling device, and supplying the gas to the at least one combustion device to generate a temperature rising function, and recycling the brine that reabsorbs heat back to the Heat exchange device. 2. The energy cycle system of claim 1, wherein the heat exchange device further comprises a refrigeration circuit and a vaporization circuit, the refrigeration circuit is configured to circulate the brine to conduct the heat, and the vaporization circuit makes the liquid This heat is absorbed to vaporize into the gas. 3. The energy cycle system of claim 2, wherein the refrigeration circuit is further coupled with at least one pump for circulating the brine. 4. The energy cycle system of claim 1, further comprising a turbine device for generating an electrical energy by driving the gas to supply the power required by the cooling device, the combustion device or an electrical device. . 5. The energy cycle system of claim 4, wherein the turbine device is a turbine engine. 6. The energy cycle system of claim 4, further comprising a liquefaction device for re-liquefying a portion of the gas into the liquid using the electrical energy or the heat lost. 7. The energy recycling system of claim 1, wherein the liquid system is a liquefied natural gas. 8. The energy recycling system of claim 1, wherein the gas system is a natural gas. The energy recycling system of claim 1, wherein the heat exchange device further comprises a storage tank for storing the liquid for providing vaporization. 10. The energy recycling system of claim 1, wherein the cooling device is an indoor air conditioner. 11. The energy recycling system of claim 1, wherein the cooling device is an air conditioner. 12. The energy recycling system of claim 1, wherein the cooling device is a refrigerator. 13. The energy cycle system of claim 1, wherein the combustion device is a gas furnace. 14. The energy cycle system of claim 1, wherein the combustion device is an indoor air conditioner. 15. The energy cycle system of claim 1, wherein the combustion device is a heater. 16. The energy cycle system of claim 1, wherein the combustion device is a water heater. 17. An energy recycling method comprising, at least: conducting heat of one of a brine by a heat exchange device to vaporize a liquid into a gas, and thereafter outputting the gas and the water that loses heat, and providing a building and Constructing an indoor circulation mechanism therein, connecting the heat exchange device, circulating the brine to provide a cooling function of at least one cooling device, and supplying the gas to at least one combustion device to generate a heating function, and recirculating the brine to re-absorb the heat Return to the heat exchange device. 18. The energy recycling method of claim 17, further comprising providing a turbine device to generate an electric 15 1298782 energy by driving the gas to supply the cooling device, the combustion device or an electrical device The power required. 19. The energy cycle method of claim 18, wherein the turbine device is a turbine engine. 20. The energy recycling method of claim 18, further comprising providing a liquefaction device that utilizes the electrical energy or loses heat of the brine to reliquefy a portion of the gas into the liquid. The energy recycling method according to claim 17, wherein the heat exchange device further comprises a refrigeration circuit and a vaporization circuit, the refrigeration circuit is configured to circulate the brine to conduct the heat, and the vaporization circuit The liquid is allowed to absorb the heat to vaporize into the gas. 22. The energy recycling method of claim 21, wherein the refrigeration circuit is further coupled to at least one pump for circulating the brine. " 23, as claimed in claim 17 of the energy circulation method, wherein the liquid system is a liquefied natural gas. 24. The energy recycling method of claim 17, wherein the gas system is a natural gas. 25. The energy recycling method of claim 17, wherein the heat exchange device further comprises a storage tank for storing the liquid for vaporization. 26. The energy recycling method according to claim 17, wherein the cooling device is an indoor air conditioner. 27. The energy recycling method of claim 17, wherein the cooling device is an air conditioner. 28. The energy recycling method of claim 17, wherein the cooling device is a refrigerator. 29. The energy recycling method according to claim 17, wherein the gas burning device is a gas burner. 30. The energy recycling method of claim 17, wherein the combustion device is an indoor air conditioner. 31. The energy recycling method of claim 17, wherein the combustion device is a heater. 32. The energy recycling method of claim 17, wherein the combustion device is a water heater. 1717
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105073573A (en) * 2013-01-25 2015-11-18 泰姆特私人有限公司 Offshore facility

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105073573A (en) * 2013-01-25 2015-11-18 泰姆特私人有限公司 Offshore facility

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