TWI281011B - Improved containers and methods for containing pressurized fluids using reinforced fibers and methods for making such containers - Google Patents

Improved containers and methods for containing pressurized fluids using reinforced fibers and methods for making such containers Download PDF

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TWI281011B
TWI281011B TW92106971A TW92106971A TWI281011B TW I281011 B TWI281011 B TW I281011B TW 92106971 A TW92106971 A TW 92106971A TW 92106971 A TW92106971 A TW 92106971A TW I281011 B TWI281011 B TW I281011B
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Taiwan
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self
sustaining
liner
container
kpa
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TW92106971A
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Chinese (zh)
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TW200404135A (en
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Moses Minta
Ronald R Bowen
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Exxonmobil Upstream Res Co
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Abstract

Containers suitable for storing pressurized fluids at cryogenic temperatures of -62 DEG C (-80 DEG F) and colder are provided and comprise a self-supporting liner and load-bearing composite overwrap, whereby means are provided for substantially preventing failure of the container during temperature changes.

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1281011 (1) 玖、發明說明 【發明所屬之技術領域】 本發明有關一種容納加壓流體之改良容器及方法,及 一種製造該容器之方法。本發明尤其有關一種包含自持性 襯墊及承載負荷之複合材料包覆層的容器,其配置裝置以 實質防止該容器於溫度在環境溫度及約-123 °c(-190 °F)之 間變化時破裂,且有關一種使用該容器容納加壓流體之方 法,及一種製造該容器之方法。部分實施例中,本發明有 關用以容器加壓液化天然氣(PLNG)之改良容器及方法。 【先前技術】 以下說明書係定義各個辭彙。爲了方便,本發明辭庫 係直接收置於申請專利範圍之前。 美國專利第6,085,528號(“PLNG專利”)標題爲”處理 、儲存及輸送液化天然氣之改良系統(Improved System for Processing, Storing, and Transporting Liquefied Natural Gas)”描述一種容器及運輸船,用於在約1 03 5 kPa (150 psi a)至約7590 kP a (1100 psi a)廣大範圍壓力及約 -123°C (-190°F )至約- 62°C (_8 0°F )廣大範圍溫度下儲存及海 上運輸加壓液化之天然氣(PLNG)。PLNG專利所描述之容 器係自超高強度、低合金鋼製得,其係含有低於9重量% 之鎳,且抗張強度大於83 0 MPa (120 ksi),而DBTT(韌性 之量度,如辭庫所定義)低於約- 73°C (-100°F )。如PLNT 專利所討論,在其中所述之較佳發明操作壓力及溫度下, -6- 1281011 (2) 約3V2重量%之鎳鋼可使用於PLNG工廠之最冷操作區中 的程序管路及設備,而習用LNG工廠(β卩,於大氣壓及 約-162°C(-260 °F)下製造LNG之工廠)中之相同設備通常 需要較昂貴之9重量%鎳鋼。較佳係使用於P L N G工廠之 操作條件下具有適當之強度及破裂韌性之低合金鋼,以構 建管路及接合組件(例如凸緣、閥、及配件)、加壓器皿、 及PLNG工廠之其他設備,以提供優於習用LNG工廠之 經濟優勢。美國專利第6,212,891號(“程序組件專利”)標 題爲”適於容納及輸送低溫流體之程序組件、容器及管路 (Process Components,Containers, and Pipes Suitable For Containing and Transporting Cryogenic Temperature Fluids)”描述適於容納及輸送低溫流體之程序組件、容器 、及管路。該程序組件專利尤其描述程序組件、容器、及 管路,其係自含有低於9重量%之鎳且具有高於83 0 MPa (120 ksi)之抗張強度及低於約-73°C(-l〇〇°F)之DBTT的超 高強度、低合金鋼構建。美國專利第6,460,72 1號(“非承 載型襯墊容器專利”)標題”製造及儲存加壓液化天然氣之 系統及方法(Systems And Methods For Producing And Storing Pressurized Liquefied Natural Gas)”描述容器及運 輸船,其用於在約 1035 kPa (150 psia)至約 7590 kPa (1 100 psia)廣大範圍壓力及約-123°C (-190°F )至約-62乞( -80 °F )廣大範圍溫度下儲存及海上運輸加壓液化之天然氣 (PLNG)。非承載型襯墊容器專利中所描述之容器係自下 列者構成(a)由複合材料製得之承載型器皿,該器皿適於 1281011 (3) 承受約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)之壓 力及約-123°C(-190T)至約-62°C(-80°F)之溫度;及(b)與 該器皿接觸之實質非承載型襯墊,該襯墊針對該加壓液化 天然氣提供實質無法滲透之障壁。 該PLNG專利及程序組件專利係採用超高強度、低合 金鋼作爲PLNG工廠與用於儲存及輸送該PLNG之容器之 間的連接主題。若使用鋼建構該容器無法提供可用於在海 上船舶上儲存及輸送PLNG之商業裝置,則該工廠中任何 鋼之應用皆無意義,因爲沒有可商業運輸該工廠所生成之 PLNG的機制。相反地,雖然在PLNG工廠中使用鋼會較 習用LNG操作具有部分經濟性,但最實質之經濟優點係 來自工廠之巨幅簡化(及後續之成本降低)。因爲其相對簡 易設計,該PLNG工廠實質上較具有相同容量之習用LNG 工廠便宜。此外,雖然PLNG輸送系統中使用鋼具有經濟 性,且確實較習用LNG操作經濟,但鋼容器之重量較其 PLNG船貨大,導致船貨裝載容量性能因子(PF)相對低。 壓縮流體儲存容器之PF與船貨對容器體積(V)所產生之壓 力(P)及容器重量(W)具有方程式PF = PV/W之關係。全鋼 PLNG系統(即工廠加輸送)目前所欠缺的是PLNG工廠與 可操作PLNG之低成本、高PF、以容器爲主之輸送系統 的組合。 使用提供高強度-重量比例之高性能纖維建構包覆有 輕質複合材料之加壓器皿。該輕質加壓器皿已廣泛使用於 航空業及維生系統,諸如專業滅火員、礦工及救援人員使 1281011 (4) 用之緊急吸呼設備。此等加壓器皿亦使用於醫藥應用及供 飛行人員及乘客使用之攜帶氧。Seal等人(美國專利第 5,82 2,8 3 8號)描述兩種使用於該高壓氣體容納系統之設計 中的主要技術。最普遍的第一種硏究係使用薄金屬襯墊( 例如鋁),於使用循環中因爲各壓力循環導致高於襯墊之 屈服應變之纖維/複合材料應變而屈服。此種情況通常限 制該襯墊之循環壽命,因此限制該加壓器皿之循環壽命。 此項硏究中,襯墊係爲非承載性;基本上不承載結構負荷 ,而僅作爲供加壓器皿使用之透氣障壁。該襯墊一般係接 合於該複合材料上。第二項硏究中,襯墊選擇於加壓期間 相對於纖維應變具有較高彈緘範圍之材料。此種情況增長 襯墊壽命,因爲該襯墊於操作壓力循環間保持彈性。該襯 墊亦需分擔結構負荷,因此具有承載之特性。該複合材料 一般僅施加於周向,因爲該襯墊需厚至足以於彈性範圍操 作。Seal等人較屬意鈦襯墊。美國專利第5,577,630號 (Blair等人)及美國專利第5,798,156號(Mitlitsky等人)皆 描述用於儲存及輸送壓縮天然氣之經襯墊、複合材料加壓 器皿。 於低溫下使用該種經複合材料包覆之加壓器皿牽#言受 計之問題,因爲襯墊材料與複合材料有CTE或熱膨S長係 數或收縮率差異。CTE之典型値在碳纖維複合材料係約 -5·6χ1 (Γ7 m/m/K (-1x1 0_6 in/in/°F ),在玻璃纖維複合材料 係約 3.3xl0·6 m/m/K (6xl(T6 in/in/°F ),而在銘係約 7·2χ10·6 m/m/K (13xl0·6 in/in/°F)。當典型複合材料加壓 1281011 (5) 器皿冷卻至低溫時,襯墊(一般爲鋁)易較複合材料材料收 縮’使得襯墊與捲繞物分離,導致過早損壞。針對CTE 問題之新穎硏究係數項專利之標的,例如美國專利第 4,8 3 5,9 75號(Brook等人)、美國專利第3,83 0,180號 (Bolton)及美國專利第4,073,400號(Brook等人)。例如 Windecker(美國專利第4,8 3 5,975號)提出使用低碳鋼襯墊 (CTE 約爲 3·1χ1〇·6 m/m/K (5·5χ10·6 in/in/°F)及玻璃纖維 複合材料,其具有同等之CTE,以避免該項問題。 美國專利第 3,8 3 0,180號(“Bolton”)討論使用雙壁複 合材料圓柱型器皿結構,以輸送一般LNG,即於大氣壓 下及約-162°C(-260°F)溫度下之LNG。然而,Bolton之器 皿的承載內壁係針對約0.34至0·41 MpA (50至60 psi)最 大壓力設計,因此,Bolton器皿不適於輸送及儲存PLNG 。此外’ Bolton未討論襯墊材料,僅提及使用塑料,諸如 FRP管路(纖維補強塑料管路)、或其他適於構成該器皿之 內外壁的材料”可於低溫下承受曝光及應力”;然而,使用 FRP必需使用襯墊,因爲FRP之樹脂會於低溫下微量龜 裂’且產物無法滲透,如同熟習此項技術者所熟知。 S.G. Ladkany,方令 Advance in Cryogenic Engineering, Materials,第28冊(第4屆國際低溫材料會議之議事記錄), San Diego,California,USA,1981 年 8 月 10 日至 1981 年 8月14日所發表之”於中間溫度下輸送LNG之複合材料 鋁-玻璃纖維環氧樹脂加壓器皿”討論用以在介於臨界條件 間之溫度及壓力條件下輸送液化天然氣(LNG)之加壓容器 -10- 1281011 (6) 的設計,191K,4.69 MPa (-116°F,680 psi)及環境條件 106 K,0.1 MPa (-268°F,14.7 psi)。Ladkany 之設計係爲 47毫米(1.85英吋)厚之鋁器皿,周圍使用17毫米(.67英 吋)厚之高強度玻璃纖維環氧樹脂層或51毫米(2英吋)厚 之拉製玻璃聚酯包覆層補強,藉由放置於2.16米(7.1英 呎)間隔下之周框針對屈曲進行強化。該強化框亦用於輸 送及操作期間於結構上支撐且固定該自行站立之器皿。使 用於周框捲繞加壓器皿之金屬襯墊因此需要抗屈曲性,而 增加了設計複雜性,且限制了加壓容器之尺寸。Ladkany 選擇焊接鋁加壓器皿,以容納中間溫度LNG。 美國專利第5,499,73 9號(Greist,III等人)討論由經修 飾耐綸6或耐綸1 1材料所製之熱塑性襯墊,其使用於加 壓器皿,以控制氣體滲透,且容許低溫操作,所陳述之低 點係爲- 40°C (-40°F )。美國專利第5,65 8,0 1 3號(Bees等人 )討論使用於交通工具之燃料槽,用於容裝及分配液體及 氣體燃料,且建議其結構中可使用完全複合材料或玻璃纖 維補強之材料。該專利所討論之液體燃料於環境溫度及壓 力下係爲習用液體燃料。前述之Bees等人及Mitlitsky等 人皆提出塗覆金屬、以聚合物爲主之襯墊,其進一步增加 瑯槽/器皿之性能因子。然而,該金屬沉積方法及襯墊製 造方法之複雜性及因而所致之高成本使得Bees等人及 Mitlitsky等人之槽/器皿主要適於最大收費容器係爲主要 物件之應用,因此,槽/器皿重量低極爲重要。美國專利 第5,69 5,8 3 9號(Yamada等人)討論一種複合材料容器,其 1281011 (7) 具有氣體障壁性質,其中用以構成該容器之包含材料係具 有層積結構,且材料層諸如鋁箔係配置或夾置於該層積結 構中。然而,此等刊物中所討論之容器中皆未設計以容裝 同時於低於-40 °C (-40 °F )之溫度及高壓下流體,諸如 PLNG之溫度及壓力。 習用液化天然氣(“LNG”)一般係於約-162°C (-260卞)溫 度及環境壓力下經海輸送,使用可用於低溫之鋁或鋼所製 得之球形或密閉成球形之槽(經常稱爲摩斯球(M〇Ss Ppheres))。此等球槽之使用壓力對於PLNG而言太低。使 用習用材料設計適於PLNG使用壓力之極大型槽因爲一般 需要極大材料厚度,而面臨了製造上之挑戰。用於如 PLNG所述般地儲存及輸送PLNG之容器係自超高強度、 低合金鋼製得。然而,儘管用於構成PLNG專利所述之 PLNG容器的鋼的高強度,使用此等容器之容納系統的重 量對於船貨而言仍相對高,經由參數諸如吃水部分及安定 性而限制了船隻設計。此外,此等容器相對於一般摩斯球 LNG容器係多爲圓柱形且直徑小,因此多需將低溫等級 材料連接於少數容器,以簡化裝貨及卸貨。此外,圓柱形 容器之配置易影響船隻之幾何設計,影響船段係數,因此 增加動力需求,防礙機房之視線。本發明所使用之船段係 數係定義爲V/(L)(B)(T),其中V係爲船所置放之流體體 積,L係爲船垂線間之長度,B係爲船幅,且T係爲船之 吃水部分。 該非承載襯墊專利提出一種具有非承載襯墊而基於輕 -12- 1281011 (8) 質' 局性能複合材料容器之備擇容納系統設計。較輕之重 量藉由去除與重量有關之限制而增進器皿之設計性。然而 ’薄內襯複合材料容器之製造複雜性限制了容器之尺寸及 幾何形狀’因而增加管線需求之複雜性,及對於管線幾何 形狀設計之衝擊性。 儘管有前述技術上之進步,即使提供了製造且儲存加 壓液化天然氣(PLNG)之系統及方法,仍以具有儲存且輸 送PLNG之改良容器及方法爲佳。 因此’本發明目的係提出該種改良之容器及方法。本 發明之其他目的可由以下發明描述而得知。 【發明內容】 本發明之一實施例中,提供一種適於儲存加壓流體之 容器,其適用於約1 0 3 5 kPa (150 psia)至約 7 5 90 kPa (1 100 psia)之壓力及約-123°C (-190°F )至約- 62°C (-80°F )之 溫度,該容器係包含:(a) —自持性襯墊,該自持性襯墊 係針對該加壓流體提供實質不可滲透之障壁;及(b) —承 載器皿,與該自持性襯墊接觸,該承載器皿係自複合材料 製得,且適於承受約 1 03 5 kPa (150 psia)至約75 90 kPa (1 100 psia)之壓力及約-123°C (-190°F )至約-62°C (-80°F )之 溫度,且該複合材料具有一熱膨脹係數,其(i)實質上與位 於該自持性襯墊界面之自持性襯墊的熱膨脹係數相同,且 (ii)其跨經該承載器皿之厚度隨著與該界面之距離的增加 而逐漸降低。於一實施例中,該容器之承載器皿具有一最 -13- 1281011 (9) 外層包覆層’基本上係由碳纖維或提供類似碳纖維所提供 之潛變性能的材料所構成。另一實施例中,該容器之元件 (b)係由下列者置換:(b)一承載器皿,與該自持性襯墊接 觸’該承載器皿係自複合材料製得,且適於承受約103 5 kPa (150 psia)至約 7590 kPa (1100 psia)之壓力及約-123 t(-190°F)至約-62°C(-80°F)之溫度,該複合材料係包含 位於該自持性襯墊界面上之中間材料,其中該中間材料具 有適當之抗切強度或應變,以實質防止該容器於溫度在環 境溫度及約-123°C (」90°F )之間變化時損壞。另一實施例 中,該容器之自持性襯墊係由基本上由鋁組成之材料製得 ’且元件(b)係由下列者置換:(b)承載器皿,與該自持性 襯墊接觸,該承載器皿係自複合材料製得,且適於承受約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)之壓力及 約-123°C(_190°F)至約-62°C(-80°F)之溫度,該複合材料係 包含選自下列者之纖維⑴碳,(ii)玻璃,(iii)凱夫拉爾 (kevlar),(iv)芳族聚醯胺,及(v)超高分子量聚乙烯。另 一實施例中,該容器之自持性襯墊係由基本上由鋼組成之 材料製得,其屈服強度至少約690 MPa (100 ksi),其基材 及焊接後之受熱區中的延性-脆性轉變溫度低於約-62 °C ( -80°F ),且元件(b)係由下列者置換:(b)承載器皿,與該 自持性襯墊接觸,該承載器皿係自複合材料製得,且適於 承受約 1 03 5 kPa (150 psia)至約 7590 kPa (1100 psia)之壓 力及約-123°C(-190°F)至約-62t(-80°F)之溫度,該複合材 料係包含選自下列者之纖維(i)碳,(i i)玻璃,(i i i)凯夫拉 -14- 1281011 (10) 爾(kevlar),(iv)芳族聚醯胺,及(v)超高分子量聚乙烯。 本發明另一實施例中,提供一種適於在約1 03 5 kPa (15 0 psia)至約 75 90 kPa (1 100 psia)之壓力及約-123°C ( _190°F )至約-62°C (-80°F )之溫度下儲存加壓液化天然氣之 容器,該容器係包含:(a) —自持性襯墊,該自持性襯墊 係針對該加壓流體提供實質不可滲透之障壁;及(b) —承 載器皿,與該自持性襯墊接觸,該承載器皿係自複合材料 製得,且適於承受約 1 03 5 kPa (150 psia)至約 75 90 kPa (1 100 psia)之壓力及約-123°C (-190°F )至約- 62°C (-80°F )之 溫度,且該複合材料具有實質上與位於該自持性襯墊界面 之自持性襯墊的熱膨脹係數相同熱膨脹係數。 亦提供一種製造容器之方法,該容器適用於約1035 kPa (150 psia)至約 7590 kPa (1100 psia)之壓力及約-123 °C (-190°F )至約-62\: (-8 0°F )之溫度下儲存加壓流體,該 方法包括下列步驟:(a)建構一自持性襯墊,該自持性襯 墊適於針對該加壓流體提供實質不可滲透之障壁;及(b) 使用適當之複合材料包覆該自持性襯墊,以形成一承載器 皿,其與該自持性襯墊接觸,該承載器皿適於承受約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)之壓力及 約-123°C(-190°F)至約-62°C(-80°F)之溫度,且該複合材料 具有一熱膨脹係數,其(i)實質上與位於該自持性襯墊界面 之自持性襯墊的熱膨脹係數相同,且(ii)其跨經該承載器 皿之厚度隨著與該界面之距離的增加而逐漸降低。另~實 施例中,該方法之步驟(b)係由下列者置換:(b)使用適當 -15- 1281011 (11) 之複合材料包覆該自持性襯墊,以形成與該自持性襯墊接 觸之承載器皿,該承載器皿適於承受約1035 kPa (150 psia)至約 7 5 90 kPa (1100 psia)之壓力及約-123°C(-190T) 至約-62°C(-80°F)之溫度,且該複合材料係包含位於該自 持性襯墊界面上之中間材料,其中該中間材料具有適當之 抗切強度或應變,以實質防止該容器於溫度在環境及約 -1 2 3 °C (-1 9 0 °F )之間變化時損壞。該方法之另一實施例中 ’步驟(a)之自持性襯墊係由基本上由鋁組成之材料製得 ’且步驟(b)係由下列者置換:(b)使用適當之複合材料包 覆該自持性襯墊,以形成與該自持性襯墊接觸之承載器皿 ,該承載器皿適於承受約1 03 5 kPa (150 psia)至約75 90 kPa (1100 psia)之壓力及約 _i23°C(-190°F)至約- 62°C(-80 °F )之溫度,該複合材料係包含選自下列者之纖維(i)碳, (ii)玻璃,(iii)凱夫拉爾(kevlar),(iv)芳族聚醯胺,及(v) 超高分子量聚乙烯。該方法之另一實施例中,步驟(a)之 自持性襯墊係由基本上由鋼組成之材料製得,其屈服強度 至少約690 MPa (100 ksi),其基材及焊接後之受熱區中的 延性-脆性轉變溫度低於約-62 °C (-80 T ),且步驟(b)係由 下列者置換:(b)使用適當之複合材料包覆該自持性襯墊 ’以形成與該自持性襯墊接觸之承載器皿,該承載器皿適 於承受約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)之 壓力及約-123°C(-190°F)至約-62°C(-80°F)之溫度,該複合 材料係包含選自下列者之纖維(i)碳,(ii)玻璃,(iii)凱夫 拉爾(kevlar),(iv)芳族聚醯胺,及(v)超高分子量聚乙烯 -16- 1281011 (12) 亦提供一種製造容器之方法,該容器適用於約1035 kPa (150 psia)至約 7 5 90 kPa (1100 psia)之壓力及約-123 t (-19 0°F )至約- 62°C (-8 0°F )之溫度下儲存加壓液化天然 氣,該方法包括下列步驟:(a)建構一自持性襯墊,該自 持性襯墊適於針對該加壓流體提供實質不可滲透之障壁; 及(b)使用適當之複合材料包覆該自持性襯墊,以形成一 承載器皿,其與該自持性襯墊接觸,該承載器皿適於承受 約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)之壓力及 約-123°C(-190°F)至約-62°C(-80°F)之溫度,且該複合材料 具有實質上與位於該自持性襯墊界面之自持性襯墊的熱膨 脹係數相同之熱膨脹係數。 本發明另一具體實例中,提供一種於約1 03 5 kPa (150 psia)至約 7590 kPa (1100 psia)之壓力及約-123°C(-190°F )至約- 62°C (-8 0°F )之溫度下儲存加壓液化天然氣之 方法,該方法包括下列步驟:將該加壓液化天然氣安裝於 至少一容器中,該至少一容器係包含(a)—自持性襯墊, 該自持性襯墊係針對該加壓流體提供實質不可滲透之障壁 :及(b)—承載器皿,與該自持性襯墊接觸,該承載器皿 係自複合材料製得,且適於承受約1 03 5 kPa (150 psia)至 約 7590 kPa (1100 psia)之壓力及約-123 °C (-190 °F)至約 •62°C(-80°F)之溫度,且該複合材料具有實質上與位於該 自持性襯墊界面之自持性襯墊的熱膨脹係數相同之熱膨脹 係數。該方法之另一實施例中,該至少一容器係包含(a) -17- 1281011 (13) 一自持性襯墊,該自持性襯墊係針對該加壓流體提供實質 不可滲透之障壁;及(b)—承載器皿,與該自持性襯墊接 觸,該承載器皿係自複合材料製得,且適於承受約1035 kPa (150 psia)至約 7 5 90 kPa (1100 psia)之壓力及約-123 °C(-190°F)至約-621(-8(^)之溫度,且該複合材料具有 一熱膨脹係數,其(i)實質上與位於該自持性襯墊界面之自 持性襯墊的熱膨脹係數相同,且(ii)其跨經該承載器皿之 厚度隨著與該界面之距離的增加而逐漸降低。該方法之另 一實施例中,該至少一容器係包含(a)—自持性襯墊,該 自持性襯墊係針對該加壓流體提供實質不可滲透之障壁; 及(b) —承載器皿,與該自持性襯墊接觸,該承載器皿係 自複合材料製得,且適於承受約1035 kPa (150 psia)至約1281011 (1) Description of the Invention [Technical Field] The present invention relates to an improved container and method for containing a pressurized fluid, and a method of manufacturing the same. More particularly, the present invention relates to a container comprising a self-sustaining liner and a load-bearing composite coating disposed to substantially prevent the container from changing between ambient temperature and about -123 ° C (-190 ° F). Time rupture, and a method of using the container to contain a pressurized fluid, and a method of making the container. In some embodiments, the present invention relates to improved containers and methods for use in pressurized liquefied natural gas (PLNG) containers. [Prior Art] The following specification defines each vocabulary. For convenience, the lexicon of the present invention is directly received before the scope of the patent application. U.S. Patent No. 6,085,528 ("PLNG Patent") entitled "Improved System for Processing, Storing, and Transporting Liquefied Natural Gas" describes a container and a transport vessel for use in 1 03 5 kPa (150 psi a) to approximately 7590 kP a (1100 psi a) for a wide range of pressures and temperatures ranging from approximately -123 ° C (-190 ° F) to approximately - 62 ° C (_8 0 ° F) Storage and marine transportation of pressurized liquefied natural gas (PLNG). The container described in the PLNG patent is made from ultra high strength, low alloy steel which contains less than 9% by weight of nickel and has a tensile strength greater than 83 0 MPa (120 ksi), while DBTT (a measure of toughness, such as The dictionary is defined as less than approximately -73 ° C (-100 ° F). As discussed in the PLNT patent, at the preferred operating pressures and temperatures described therein, -6-1281011 (2) about 3 V2 by weight of nickel steel can be used in the coldest operating zone of the PLNG plant. Equipment, while the same equipment in the conventional LNG plant (β卩, a plant that produces LNG at atmospheric pressure and about -162 °C (-260 °F)) typically requires a relatively expensive 9 wt% nickel steel. It is preferred to use low alloy steels with appropriate strength and fracture toughness under the operating conditions of PLNG plants to construct piping and joint components (such as flanges, valves, and fittings), pressurized vessels, and other PLNG plants. Equipment to provide economic advantages over conventional LNG plants. U.S. Patent No. 6,212,891 ("Processing Module Patent") is entitled "Process Components, Containers, and Pipes Suitable For Containing and Transporting Cryogenic Temperature Fluids". Program components, containers, and tubing for containing and transporting cryogenic fluids. The program component patent particularly describes program components, vessels, and tubing that contain less than 9% by weight nickel and have a tensile strength above 83 0 MPa (120 ksi) and less than about -73 ° C ( -l〇〇°F) DBTT ultra high strength, low alloy steel construction. U.S. Patent No. 6,460,72 ("Unloaded Pad Container Patent") "Systems and Methods For Producing And Storing Pressurized Liquefied Natural Gas" describes containers and transportation The vessel is used for a wide range of pressures from about 1035 kPa (150 psia) to about 7590 kPa (1 100 psia) and a wide range of about -123 ° C (-190 ° F ) to about -62 乞 ( -80 ° F ) Storage and maritime transport of pressurized liquefied natural gas (PLNG) at temperatures. The container described in the non-load bearing liner container is constructed from (a) a carrier-type vessel made of a composite material suitable for 1281011 (3) to withstand about 1 03 5 kPa (150 psia) to about a pressure of 75 90 kPa (1100 psia) and a temperature of about -123 ° C (-190 T) to about -62 ° C (-80 ° F); and (b) a substantially non-loading liner in contact with the vessel, The liner provides a substantially impenetrable barrier to the pressurized liquefied natural gas. The PLNG patent and program component patents use ultra-high strength, low alloy steel as the subject of connection between the PLNG plant and the container for storing and transporting the PLNG. If the construction of the container using steel does not provide a commercial unit for storing and transporting PLNG on a ship on the sea, then the application of any steel in the plant is meaningless because there is no mechanism to commercially transport the PLNG generated by the plant. Conversely, while the use of steel in a PLNG plant is somewhat economical than the LNG operation, the most substantial economic advantage comes from the simplification of the plant (and subsequent cost reductions). Because of its relatively simple design, the PLNG plant is essentially less expensive than a conventional LNG plant of the same capacity. In addition, although the use of steel in PLNG conveyor systems is economical and indeed economical compared to conventional LNG operations, the weight of steel containers is greater than that of PLNG cargoes, resulting in a relatively low cargo load capacity performance factor (PF). The pressure (P) and the container weight (W) generated by the PF of the compressed fluid storage container versus the volume (V) of the container have the relationship of equation PF = PV/W. What is currently lacking in all-steel PLNG systems (ie, factory plus transport) is the combination of a low-cost, high-PF, container-based conveyor system for PLNG plants and operational PLNG. A pressurized vessel coated with a lightweight composite is constructed using high performance fibers that provide a high strength-to-weight ratio. This lightweight pressurizing vessel has been widely used in the aviation industry and in life-sustaining systems, such as emergency fire-fighting equipment used by professional firefighters, miners and rescuers to make 1281011 (4). These pressurized vessels are also used in medical applications and for carrying oxygen for flight crews and passengers. Seal et al. (U.S. Patent No. 5,82 2,8 3 8) describe two main techniques used in the design of the high pressure gas containment system. The most common first type of study uses thin metal liners (e.g., aluminum) that yield in the use cycle due to various pressure cycles resulting in fiber/composite strain above the yield strain of the liner. This condition typically limits the cycle life of the liner, thus limiting the cycle life of the pressurized vessel. In this study, the liner is unloaded; it does not carry structural loads, but only serves as a gas barrier for pressurized vessels. The liner is typically attached to the composite. In the second study, the liner was selected to have a higher elastic range relative to fiber strain during pressurization. This condition increases the life of the liner because the liner remains resilient between operating pressure cycles. The lining also needs to share the structural load and therefore has the characteristics of carrying. The composite is typically applied only in the circumferential direction because the liner needs to be thick enough to operate in the elastic range. Seal et al. prefer a titanium liner. U.S. Patent Nos. 5,577,630 (Blair et al.) and U.S. Patent No. 5,798,156 (Mitlitsky et al.), each of which are incorporated herein by reference. The use of such a composite-coated pressurized vessel at low temperatures is a problem because the gasket material and the composite material have a difference in CTE or thermal expansion S length or shrinkage. The typical enthalpy of CTE is about -5·6χ1 (Γ7 m/m/K (-1x1 0_6 in/in/°F) in carbon fiber composites and about 3.3xl0·6 m/m/K in glass fiber composites ( 6xl (T6 in/in/°F), and in the case of about 7·2χ10·6 m/m/K (13xl0·6 in/in/°F). When the typical composite is pressurized, 1281011 (5) is cooled by the vessel. At low temperatures, the liner (usually aluminum) tends to shrink more than the composite material', causing the liner to separate from the winding, causing premature failure. The novelty of the CTE problem is patented, for example, US Patent No. 4 , 8 3 5, 9 75 (Brook et al.), U.S. Patent No. 3,83,0,180 (Bolton), and U.S. Patent No. 4,073,400 (Brook et al.), for example, Windecker (U.S. Patent No. 4,8 3 5,975) No.) proposes the use of low carbon steel liners (CTE approximately 3·1χ1〇·6 m/m/K (5·5χ10·6 in/in/°F) and fiberglass composites with equivalent CTE to Avoid this problem. US Patent No. 3,8 3 0,180 ("Bolton") discusses the use of a double-walled composite cylindrical vessel structure to deliver general LNG at atmospheric pressure and at about -162 ° C (-260 °F) LNG at temperature. However, the bearing inner wall of Bolton's vessels is designed for a maximum pressure of about 0.34 to 0.41 MpA (50 to 60 psi), so Bolton vessels are not suitable for transporting and storing PLNG. In addition, 'Bolton did not discuss liner materials, only mention And the use of plastics, such as FRP tubing (fiber-reinforced plastic tubing), or other materials suitable for forming the inner and outer walls of the vessel "can withstand exposure and stress at low temperatures"; however, the use of FRP requires the use of gaskets because of FRP The resin will be slightly cracked at low temperatures and the product will be impermeable, as is well known to those skilled in the art. SG Ladkany, Advance in Cryogenic Engineering, Materials, Vol. 28 (Proceedings of the 4th International Conference on Low Temperature Materials) ), San Diego, California, USA, "Aluminum-glass fiber epoxy resin pressurized vessels for transporting LNG at intermediate temperatures" published from August 10, 1981 to August 14, 1981 Design of pressurized container for transporting liquefied natural gas (LNG) under temperature and pressure conditions between critical conditions -10- 1281011 (6), 191K, 4.69 MPa (-116°F, 680 psi) Environmental conditions 106 K, 0.1 MPa (-268 ° F, 14.7 psi). The Ladkany design is a 47 mm (1.85 inch) thick aluminum vessel surrounded by a 17 mm (.67 inch) thick high strength fiberglass epoxy layer or a 51 mm (2 inch) thick drawn glass. The polyester coating was reinforced and strengthened for buckling by a perimeter frame placed at a spacing of 2.16 meters (7.1 inches). The reinforced frame is also used to structurally support and secure the self-standing vessel during transport and operation. The metal liner used for the circumferential frame winding of the pressure vessel thus requires buckling resistance, which increases design complexity and limits the size of the pressurized container. Ladkany chose to weld aluminum pressurization vessels to accommodate the intermediate temperature LNG. U.S. Patent No. 5,499,73 (Greist, III et al.) discusses the use of a thermoplastic liner made of a modified nylon 6 or nylon 11 material for use in pressurized vessels to control gas permeation and to allow for low temperatures. For operation, the stated low point is -40 ° C (-40 ° F). U.S. Patent No. 5,65,013 (Bees et al.) discusses fuel tanks used in vehicles for the containment and distribution of liquid and gaseous fuels, and it is suggested that a complete composite or fiberglass can be used in the construction. Reinforce the material. The liquid fuel discussed in this patent is a conventional liquid fuel at ambient temperature and pressure. Both Bees et al. and Mitlitsky et al. have proposed metal coated, polymer based liners which further increase the performance factor of the gutter/ware. However, the complexity of the metal deposition method and the method of manufacturing the liner and the resulting high cost make the tank/ware of Bees et al. and Mitlitsky et al. mainly suitable for the application of the largest toll container as the main object, therefore, the tank/ The low weight of the vessel is extremely important. U.S. Patent No. 5,69,5,8,9 (Yamada et al.) discusses a composite container having 1281011 (7) having gas barrier properties, wherein the materials used to construct the container have a laminated structure and materials A layer such as an aluminum foil is disposed or sandwiched in the laminated structure. However, none of the vessels discussed in these publications are designed to accommodate fluids at temperatures below -40 °C (-40 °F) and high pressures, such as the temperature and pressure of PLNG. Conventional liquefied natural gas ("LNG") is generally transported by sea at a temperature of about -162 ° C (-260 Torr) and at ambient pressure, using spherical or closed spherical grooves made of aluminum or steel for low temperature ( Often referred to as M〇Ss Ppheres). The use pressure of these ball slots is too low for PLNG. The use of conventional materials to design extremely large grooves suitable for the use of PLNG is faced with manufacturing challenges because it generally requires a very large material thickness. Containers for storing and transporting PLNG as described in PLNG are made from ultra high strength, low alloy steel. However, despite the high strength of the steel used to construct the PLNG container described in the PLNG patent, the weight of the containment system using such containers is relatively high for cargo, limiting vessel design via parameters such as draft and stability. . In addition, these containers are mostly cylindrical and have a small diameter relative to a typical Moss LNG container system, so it is often necessary to connect low temperature grade materials to a small number of containers to simplify loading and unloading. In addition, the configuration of the cylindrical container is susceptible to the geometric design of the vessel, affecting the segment coefficient, thus increasing the power demand and obstructing the view of the machine room. The coefficient of the ship segment used in the present invention is defined as V/(L)(B)(T), where V is the volume of the fluid placed by the ship, L is the length between the vertical lines of the ship, and B is the width of the ship. And the T system is the draft of the ship. The non-load bearing pad patent proposes an alternative containment system design based on a lightweight -12-1281011 (8) quality composite container with a non-load bearing pad. The lighter weight enhances the design of the vessel by removing weight-related limitations. However, the manufacturing complexity of a thin lining composite container limits the size and geometry of the container' thus increasing the complexity of the pipeline requirements and the impact on the pipeline geometry design. Despite the foregoing advances in technology, even though systems and methods for manufacturing and storing pressurized liquefied natural gas (PLNG) are provided, improved containers and methods for storing and transporting PLNG are preferred. Accordingly, the object of the present invention is to provide such an improved container and method. Other objects of the invention will be apparent from the description of the invention below. SUMMARY OF THE INVENTION In one embodiment of the present invention, a container suitable for storing a pressurized fluid is provided, which is suitable for a pressure of from about 10 3 5 kPa (150 psia) to about 7 5 90 kPa (1 100 psia) and At a temperature of from about -123 ° C (-190 ° F) to about -62 ° C (-80 ° F), the container comprises: (a) a self-sustaining liner for which the self-sustaining liner is applied The fluid provides a substantially impermeable barrier; and (b) a carrier vessel in contact with the self-sustaining liner, the carrier being fabricated from a composite material and adapted to withstand from about 1 03 5 kPa (150 psia) to about 75 a pressure of 90 kPa (1 100 psia) and a temperature of about -123 ° C (-190 ° F ) to about -62 ° C (-80 ° F ), and the composite has a coefficient of thermal expansion, (i) substantial The coefficient of thermal expansion is the same as the self-sustaining pad at the self-sustaining pad interface, and (ii) the thickness across the carrier vessel gradually decreases as the distance from the interface increases. In one embodiment, the container of the container has a topmost layer of -13 - 1281011 (9) and the outer cover layer is constructed substantially of carbon fiber or a material that provides creep properties similar to those provided by carbon fibers. In another embodiment, the component (b) of the container is replaced by: (b) a carrier vessel in contact with the self-sustaining liner. The carrier vessel is made from a composite material and is adapted to withstand about 103 5 kPa (150 psia) to a pressure of about 7590 kPa (1100 psia) and a temperature of about -123 t (-190 °F) to about -62 ° C (-80 ° F), the composite material is included in the self-sustaining An intermediate material on the interface of the liner, wherein the intermediate material has suitable shear strength or strain to substantially prevent damage to the container when the temperature changes between ambient temperature and about -123 ° C ("90 ° F ). In another embodiment, the self-sustaining liner of the container is made of a material consisting essentially of aluminum and the element (b) is replaced by: (b) a carrier vessel in contact with the self-sustaining liner, The carrier vessel is made from a composite material and is adapted to withstand a pressure of from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1100 psia) and from about -123 ° C (_190 ° F) to about -62 °. C (-80 °F), the composite material comprises fibers (1) carbon selected from the group consisting of (ii) glass, (iii) kevlar, (iv) aromatic polyamines, and v) Ultra high molecular weight polyethylene. In another embodiment, the self-sustaining liner of the container is made of a material consisting essentially of steel having a yield strength of at least about 690 MPa (100 ksi), the substrate and the ductility in the heated zone after welding - The brittle transition temperature is less than about -62 °C (-80 °F), and element (b) is replaced by: (b) a carrier vessel in contact with the self-sustaining liner, the carrier being made from a composite material And suitable for withstanding a pressure of from about 1 03 5 kPa (150 psia) to about 7590 kPa (1100 psia) and a temperature of from about -123 ° C (-190 ° F) to about -62 t (-80 ° F), The composite material comprises fibers (i) carbon selected from the group consisting of (ii) glass, (iii) Kevlar-14-1281011 (10) kevlar, (iv) aromatic polyamines, and v) Ultra high molecular weight polyethylene. In another embodiment of the invention, a pressure suitable for from about 1 03 5 kPa (15 0 psia) to about 75 90 kPa (1 100 psia) and from about -123 ° C ( _190 ° F ) to about -62 is provided. A container for pressurized liquefied natural gas at a temperature of °C (-80 °F), the container comprising: (a) a self-sustaining liner that provides a substantially impermeable barrier to the pressurized fluid And (b) a carrier vessel in contact with the self-sustaining liner, the carrier being made from a composite material and adapted to withstand from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1 100 psia) Pressure and a temperature of from about -123 ° C (-190 ° F) to about -62 ° C (-80 ° F), and the composite material has substantially a self-sustaining gasket at the interface of the self-sustaining gasket The coefficient of thermal expansion is the same as the coefficient of thermal expansion. Also provided is a method of making a container suitable for a pressure of from about 1035 kPa (150 psia) to about 7590 kPa (1100 psia) and from about -123 °C (-190 °F) to about -62\: (-8 Storing a pressurized fluid at a temperature of 0 °F), the method comprising the steps of: (a) constructing a self-contained liner adapted to provide a substantially impermeable barrier to the pressurized fluid; and (b Covering the self-sustaining liner with a suitable composite material to form a carrier that is in contact with the self-sustaining liner that is adapted to withstand from about 1 03 5 kPa (150 psia) to about 75 90 kPa ( a pressure of 1100 psia) and a temperature of from about -123 ° C (-190 ° F) to about -62 ° C (-80 ° F), and the composite material has a coefficient of thermal expansion, (i) substantially The self-sustaining pad of the self-sustaining pad interface has the same coefficient of thermal expansion, and (ii) its thickness across the carrier vessel gradually decreases as the distance from the interface increases. In another embodiment, step (b) of the method is replaced by: (b) coating the self-sustaining liner with a composite material of appropriate -15-1281011 (11) to form a self-sustaining liner Contact carrier, the carrier is adapted to withstand a pressure of from about 1035 kPa (150 psia) to about 7 5 90 kPa (1100 psia) and from about -123 ° C (-190 T) to about -62 ° C (-80 ° F) the temperature, and the composite material comprises an intermediate material at the interface of the self-sustaining liner, wherein the intermediate material has suitable shear strength or strain to substantially prevent the container from being at ambient temperature and about -1 2 Damaged when changing between 3 °C (-1 90 °F). In another embodiment of the method, the self-sustaining liner of step (a) is made of a material consisting essentially of aluminum and the step (b) is replaced by: (b) using a suitable composite package Covering the self-contained liner to form a carrier vessel in contact with the self-sustaining liner, the carrier vessel being adapted to withstand a pressure of from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1100 psia) and about _i23 From °C (-190 °F) to a temperature of about -62 °C (-80 °F), the composite material comprises fibers selected from the group consisting of (i) carbon, (ii) glass, (iii) Kevlar. (kevlar), (iv) aromatic polyamines, and (v) ultrahigh molecular weight polyethylene. In another embodiment of the method, the self-sustaining liner of step (a) is made of a material consisting essentially of steel having a yield strength of at least about 690 MPa (100 ksi), the substrate and the heat after welding. The ductile-brittle transition temperature in the zone is less than about -62 °C (-80 T), and step (b) is replaced by: (b) coating the self-sustaining liner with a suitable composite material to form a carrier vessel in contact with the self-sustaining liner, the carrier vessel being adapted to withstand a pressure of from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1100 psia) and about -123 ° C (-190 ° F) to At a temperature of about -62 ° C (-80 ° F), the composite material comprises fibers selected from the group consisting of (i) carbon, (ii) glass, (iii) kevlar, (iv) aromatic Polyamide, and (v) ultra high molecular weight polyethylene-16-1281011 (12) also provides a method of making a container suitable for use from about 1035 kPa (150 psia) to about 7 5 90 kPa (1100 psia) Pressure and storage of pressurized liquefied natural gas at a temperature of about -123 t (-19 ° ° F) to about -62 ° C (-8 0 ° F), the method comprising the steps of: (a) constructing a self-sustaining gasket , the a self-contained liner adapted to provide a substantially impermeable barrier to the pressurized fluid; and (b) coating the self-sustaining liner with a suitable composite material to form a carrier vessel that is in contact with the self-sustaining liner The carrier vessel is adapted to withstand a pressure of from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1100 psia) and from about -123 ° C (-190 ° F) to about -62 ° C (-80 ° F) The temperature, and the composite has a coefficient of thermal expansion that is substantially the same as the coefficient of thermal expansion of the self-sustaining liner at the interface of the self-sustaining liner. In another embodiment of the invention, a pressure of from about 1 03 5 kPa (150 psia) to about 7590 kPa (1100 psia) and from about -123 ° C (-190 ° F) to about - 62 ° C (- A method of storing pressurized liquefied natural gas at a temperature of 80 °F, the method comprising the steps of: installing the pressurized liquefied natural gas in at least one container, the at least one container comprising (a) a self-sustaining gasket, The self-sustaining liner provides a substantially impermeable barrier to the pressurized fluid: and (b) a carrier vessel in contact with the self-sustaining liner, the carrier being fabricated from a composite material and adapted to withstand about 1 03 5 kPa (150 psia) to a pressure of about 7590 kPa (1100 psia) and a temperature of about -123 °C (-190 °F) to about 62 °C (-80 °F), and the composite has substantial The coefficient of thermal expansion is the same as the coefficient of thermal expansion of the self-sustaining pad at the self-sustaining pad interface. In another embodiment of the method, the at least one container comprises (a) -17- 1281011 (13) a self-sustaining liner that provides a substantially impermeable barrier to the pressurized fluid; (b) a carrier vessel in contact with the self-sustaining liner, the carrier being made from a composite material and adapted to withstand a pressure of from about 1035 kPa (150 psia) to about 75 5 kPa (1100 psia) and about -123 °C (-190 °F) to a temperature of about -621 (-8 (^), and the composite has a coefficient of thermal expansion, (i) substantially in self-sustaining lining at the interface of the self-sustaining pad The pad has the same coefficient of thermal expansion, and (ii) its thickness across the carrier vessel gradually decreases as the distance from the interface increases. In another embodiment of the method, the at least one container comprises (a)- a self-contained liner that provides a substantially impermeable barrier to the pressurized fluid; and (b) a carrier vessel in contact with the self-sustaining liner, the carrier being fabricated from a composite material, and Suitable to withstand approximately 1035 kPa (150 psia) to approximately

7 5 90 kPa (1 100 psia)之壓力及約-123°C (-190°F )至約-62°C (-8 0 °F )之溫度,且該複合材料係包含位於該自持性襯墊 界面上之中間材料,其中該中間材料具有適當之抗切強度 或應變,以實質防止該容器於溫度在環境溫度及約23它 (-1 9 0 °F )之間變化時損壞。該方法之另一實施例中,該至 少一容器係包含(a) —自持性襯墊,由基本上由鋁組成之 材料製得’且針對該加壓流體提供實質不可滲透之障壁; 及(b)—承載器皿’與該自持性襯墊接觸,該承載器皿係 自複合材料製得,且適於承受約1 03 5 kPa (150 psia)至約a pressure of 7 5 90 kPa (1 100 psia) and a temperature of about -123 ° C (-190 ° F ) to about -62 ° C (-8 0 ° F ), and the composite material is contained in the self-sustaining lining An intermediate material on the pad interface, wherein the intermediate material has suitable shear strength or strain to substantially prevent damage to the container when the temperature changes between ambient temperature and about 23 (-1900 °F). In another embodiment of the method, the at least one container comprises (a) a self-sustaining liner made of a material consisting essentially of aluminum and providing a substantially impermeable barrier to the pressurized fluid; b) - the carrier vessel is in contact with the self-sustaining liner, the carrier vessel being made from a composite material and adapted to withstand from about 1 03 5 kPa (150 psia) to about

75 90 kPa (1100 psia)之壓力及約-123°C(-190°F)至約-62°C (-8 0 °F )之溫度,該複合材料係包含選自下列者之纖維(i) 碳’(ii)玻璃’(iii)凱夫拉爾(kevlar),(iv)芳族聚醯胺, 1281011 (14) 及(v)超高分子量聚乙烯。該方法另一實施例中,該至少 一容器係包含(a)—自持性襯墊,由基本上由鋼組成之材 料製得,其屈服強度至少約690 MPa (100 ksi),且基材及 焊接後之受熱區中的延性-脆性轉變溫度低於約-62 °C (-80 °F ),而針對該加壓流體提供實質不可滲透之障壁;及(b) 一承載器皿,與該自持性襯墊接觸,該承載器皿係自複合 材料製得,且適於承受約1 03 5 kPa (150 psia)至約7590 kPa (1100 psia)之壓力及約-123°(:(-190°?)至約-62°(:(-80 °F )之溫度,該複合材料係包含選自下列者之纖維(i)碳, (Π)玻璃’(iii)凱夫拉爾(kevlar),(iv)芳族聚醯胺,及(v) 超高分子量聚乙烯。 與使用非承載襯墊之習用硏究不同地,本發明之容器 設計使用自持性金屬襯墊,包覆以含有低溫樹脂之高性能 複合材料纖維。本發明針對襯墊所使用之,,自持性,,係意指 可保持其結構完整性’同時支撐其自身重量。一旦施加覆 層’則該複合材料對容器提供附加之抗屈曲性。例如,參 照圖6 ’其係具有以毫米表示襯墊厚度之橫座標6〇,及以 每平方英吋磅數表示收縮壓力之縱座標61的圖,線62係 表不臨界壓力線’線6 3係表示具有1 〇米直徑之襯墊的收 縮壓力,線6 4係表示直徑2 〇米(6 5 · 6英呎)之襯墊的收縮 壓力’且線65表示直徑40米(131.2英呎)的襯墊之收縮 壓力。除收縮壓力之外的其他標準可用以決定容器襯墊是 否爲自持性,如同熟習此項技術者所熟知。本發明針對複 合材料或纖維所使用之,,高性能,,意指抗拉強度大於約 -19- 1281011 (15) 340 1 MPa(500 ksi)且模數大於約1 3 6054 MPa (20百萬磅 每平方英吋(msi))。一實施例係包括一基本LNG球形槽 ,包覆有高性能複合材料,提供PLNG容納所需之結構完 整性。本發明之優點及特性係更明確描述於下文。 襯墊本身針對纖維張力提供主要結構支撐性,因其係 捲繞於該襯墊上。捲繞於襯墊上之纖維貢獻該支撐力。該 襯墊可承受部分來自該容器中所容納之加壓、低溫流體的 負荷。如熟習此項技術者所熟知,設計細節諸如襯墊厚度 、或該襯墊所承載之負荷百分比係由熟習此項技術者根據 包含襯墊及複合材料包覆層之材料且根據熟習此項技術者 所熟知之其他因數決定。 其次,提供數項用以解決該金屬襯墊與複合材料間之 CTE差異的設計硏究。於一實施例中,CTE差異係使用中 間基質-纖維材料分度,該材料係具有實質上與襯墊界面 之襯墊CTE相同之CTE,距離襯墊愈遠,貝[J CTE愈低。 於一實施例中,最外層包覆層基本上係由碳纖維組成,用 以變善潛變特性,或基本上由提供如同碳纖維之潛變特性 的材料所組成。該基質-纖維材料設計係包括層內混雜纖 維混合物,其中碳及玻璃纖維係混合於該層內(或纖維束) 。此者具有達到良好之複合材料壓縮性的附加優點。此種 混雜物硏究的變化係層內混合,以使用交替之不同纖維層 。第三種變化係包括層積物的不同樹脂比例:與襯墊相鄰 之層積具有高於較遠離襯墊之層積物的樹脂比例,而最遠 離該襯墊之層積物中的樹脂比例係隨著與襯墊之距離的增 1281011 (16) 加而逐漸降低。該樹脂特別可調配經調整之CTE性質, 以增進複合材料或層積物之各層的性能。若使用鋁襯墊, 則此項硏究確認鋁與碳纖維(因爲較佳之潛變性能而較有 利於此種設計)間的CTE有相對大之差異’及鋁與玻璃纖 維間之相對小差異。本發明所使用之”潛變”一辭係意指由 應力所致而與時間有關之應變。 另一實施例中,該自持性襯墊係設計以承受該應用之 臨界屈曲負荷。結果,該金屬襯墊與複合材料包覆層之間 的界面保持未連接。此點異於習用經襯墊複合材料容器設 計,其中非承載襯墊係使用黏著劑連接於複合材料包覆層 ,可承載該應用所產生之界面剪切;此藉由防止襯墊自複 合材料包覆層分離,而減緩襯墊損壞。 另一實施例中,最外層包覆層基本上係由用以改善潛 變性能之碳纖維或提供類似碳纖維之潛變性能的材料所組 成。主要爲玻璃纖維的中間層係放置於該最外層碳纖維包 覆層與由可使用於低溫之鋁所製的襯墊之間。使用自緊法 於襯墊中提供殘留壓縮預應力,以補償該系統之差異熱收 縮。不使用玻璃纖維中間層時,殘留壓縮預應力不足以補 償鋁與碳之間遠較爲大之差異收縮。下列使用鋁5 083 -0 之球形壓力器皿的數據係說明該點。承載34 kP a (5 ksi) 張力之界面係當壓力器皿冷卻至-95t(-140°F)時,於鋁與 碳纖維複合材料間之周圍發展出來。此係發生於自緊壓力 6.78 MPa ( 8 5 0 psig)及後續 5·1 MPa (75 0 psig)保險壓力後 產生,兩者皆於室溫下進行。在自保險壓力解除後之對應 -21 - 1281011 (17) 承載壓力係爲3 40 kPa (50 psig)壓縮。玻璃確定該界面爲 正承載壓力,以防止接合線崩裂。鋁之低屈服強度限制了 於自緊法之後在襯墊中所誘生之殘留壓縮預應力。 本發明另一實施例中,最外層包覆層基本上係由用以 改善潛變性能之碳纖維、或提供如同碳纖維之潛變性能的 材料所組成。該襯墊使用具有高屈服強度之材料,以誘導 更高之殘留壓縮預應力。此種較高之預應力基本上補償該 襯墊與碳之間的差異收縮性,而該襯墊與碳複合材料之間 基本上不需要中間材料,諸如玻璃纖維或黏著劑。除了高 屈服強度之外,該材料需具有適當之低溫韌性。該高屈服 強度材料較佳係於基材及焊接後受熱區(“HAZ”)具有至少 約690 MPa (100 ksi)之屈服強度,及低於約-62°C(-80T) 之延性-脆性轉變溫度(“DBTT”)。符合屈服強度及BDTT 要求之例示材料係討論於國際公告編號WO 99/32672、 WO 00/3 93 52、WO 99/32670、WO 00/40764、 WO 99/3267 1、WO 00/3 7689、及 WO 99/95 3 3 5 中,及美 國專利編號 625 1 1 98、6254698、60662 12、6 1 593 1 2 及 62 64 760中。可用於接合該鋼材之焊接技術係討論於國際 公告編號 WO 0 1/63 974、WO 99/05 3 3 5、及 WO 00/56498 ,及美國專利編號6114656及6336583中。其他適當之鋼 材及焊接技術可能存在或稍後發展。所有鋼材及焊接技術 皆包括於本發明範圍內。於實施方式(Detailed Description of the Invention)結尾提供非限制襯墊鋼材及 焊接實施例。 -22- 1281011 (18) 所提供之設計有數項優於習用以鋼爲主之PLNG容納 系統的優點,包括下列者:(i)製造方法簡化;(ii)容納系 統重量減輕,對於輸送船隻設計有正面影響;(iH)產物管 路要求大幅簡化;(iv)卸荷流程圖亦簡化;且(v)絕緣要求 降低。 【實施方式】 複合材料包覆層 本發明容器中複合材料包層層以提供操作負載主要結 構支擦爲佳。該複合材料包覆層較佳係爲一材料系統,於 可於低溫下使用之樹脂基質中包含高性能纖維。本發明所 使用之”低溫,,意指約_62°C (-80T )及更冷之任何溫度。該 樹脂之實例係爲CTD 525環氧低溫樹脂。本發明已設計 兩類材料系統。 第一類材料系統係包含··(i)高性能纖維,以選自下列 纖維爲佳(碳、玻璃、凯夫拉爾(kevlar)、芳族聚醯胺、 UHMWP);及(Π)熱固性樹脂(諸如CTD-525環氧低溫樹脂 )。一實施例係使用高性能碳纖維,諸如TORAY T-700、 GRAFIL 34-600 或 ZOLTEK PANEX 35,以得到較佳潛變 性能。此種第一類材料系統之特徵係爲固定CTE値。例 如,於室溫及-73 t (-100 °F )間針對碳/環氧樹脂層積物測 量之平均 CTE 値係爲 l.lxlO·7 m/m/K (0·19χ10·6 in/in/°F) 。此値一般與法與數種金屬襯墊配合,尤其是鋁及本發明 所討論之高屈服強度鋼材,即具有至少約690 MPa (100 -23- 1281011 (19) ksi)之屈服強度的鋼材。 第二類材料系統之特徵係爲可調整之CTE値,且包 含纖維(混合不同纖維,諸如玻璃及碳)與各種樹脂組合物 。該樹脂組合物可包含具有實質純度之樹脂,及設計以改 變樹脂之CTE的添加劑。藉由明智地將參數諸如纖維比 例、樹脂分率、及添加劑含量最佳化,得到較佳之CTE。 代表性測量CTE値係爲--例如不限制本發明一鋁7.2χ1(Γ6 m/m/K (13xl0·6 in/in/°F ),純樹脂 18·8χ1(Γ6 m/m/K (33·9χ10·6 in/in/°F ),且碳 1 · 1 x 1 0·7 m/m/K (0.1 9x 1 Ο·6 in/inTF )。所需之最佳化方法係熟習此項技術者所熟知, 基於欲構成之容器的所需性能參數。此外,該包覆層之不 同層積物調整至不同CTE値,導致CTE自襯墊界面至包 覆層外表面具有級度。此級度係設計以達到可接受之層積 物間應力。此可接受之値可自分析技術決定,諸如詳細之 有限元素分析(FEA分析),如熟習此項技術者所熟知。 使用第二類材料則可使用具有任何CTE特性之襯墊 材料。相反地,第一類材料之固定CTE値特性限制其使 用於具有密切配合之CTE的襯墊,諸如由INVAR所製之 襯墊。INVAR之平均 CTE値係具有如同碳之大小, 5·0χ1(Γ7 in/in/K 比 l.lxlO·7 in/in/K(0.9xl(T6 in/in/。!?比 〇·19χ10_6 irWin/°F )。本發明另一方面係於襯墊與第〜類 材料系統之間的界面上使用具有高應變能力之中間材料, 即應變能吸收能力大於約3 4焦耳每平方米(每平方英口尺 3·0χ10·3 Btu)。 -24- 1281011 (20) 金屬襯墊 本發明容器之金屬襯墊較佳係具有三項主要功能:(i) 針對所容納之流體提供不可滲透之障壁;(ii)提供於捲繞 期間因爲纖維張力所需之主要結構支撐力;及(iii)針對操 作負載提供至少部分結構支撐力。此外,該襯墊針對因 PLNG內部壓力所產生之操作負載及外加負載(諸如因器皿 移動所致)提供至少部分結構支撐力。 參照圖5,本發明容器5之一實施例係包含一複合材 料器皿12及一襯墊10,其係由實質上不可滲透之材料諸 如鋁或本發明所討論之高屈服強度鋼材製得,即具有至少 約6 90 MPa (100 ksi)之屈服強度,其針對容器5中所裝之 PLNG提供障壁。此實施例中,複合材料器皿12承受容 窃5之結構負何’包括內部壓力負何。襯塾1 0完全被複 合材料器皿12所環繞,因此係爲完全包覆之壓力器皿。 可設計周圍包覆之另一種實例,其中襯墊10之尺寸係調 整至可承載該半球部分中的全部負荷。容器5較佳係視需 要由一外塗層1 4所保護,由可保護複合材料器皿1 2防止 濕氣、酸、紫外線及其他環境有害物質之材料所製得。例 如,在不限制本發明下,外塗層1 4可由聚胺基甲酸醋製 得。容器5亦可包括承載系統。例如,可於容器5之底端 提供補強浮雕(未出示於圖5 ),以作爲與支撐裙部(未出示 於圖5)之間的界面。支撐裙部之設計可具有任何一般設 計’如同熟習此項技術者所熟知。較佳係任何附加之補強 1281011 (21) 浮雕皆整體捲繞以複合材料器皿〗2。此提供重要之經濟 ^ ’亦改善支撐系統與容器5之間的界面之結構強度及 完整性。提供噴嘴20--較佳係位於容器5之頂端…以貫穿 至容器5內,例如以負載或卸除PLNG。於一實施例中, 噴嘴20係自金屬浮雕(未出示於圖5)衍生,於捲繞構成複 合材料器皿12之複合材料之前配置。該金屬浮雕係包覆 以複合材料,提供到達容器5內部之不滲漏且高強度界面 〇 另一實施例中,本發明容器於海上運輸船90之水平 取向使得船貨體積最大化,而輸送船90有較細之船體, 如同圖7A至圖7C所說明。現在參照圖7B,水平取向之 容器92的長度較佳係界定使各容器92可於兩點例如點 93及94上獲得支撐。就PLNG運輸船90之複雜移動而 言’單純之兩點支撐系統較有利於水平取向之容器9 2, 如熟習此項技術者所熟知。如同熟習此項技術者所熟知, 該兩點支撐系統階制了容器92之長度。當設計需要之儲 存容量大於具有使用兩點支撐系統之容許長度的容器所能 提供者時,支撐系統複雜性之稍微增加可使用具有較長長 度之容器。 如圖1所示,本發明包含自持性襯墊3及複合材料包 覆層2之容器1可具有球形。容器1可包括噴嘴4,以貫 穿進入容器1內。現在參照圖2 A,本發明四球形容器2 4 裝於船22上之實施例,承載約200,000立方米之PLNG 產物’發現下列符合船及船貨要求、及前述之襯墊功能性 -26- 1281011 (22) 要求之襯墊幾何參數: 直徑一約46米(150.9英呎) 襯墊材料一鋁合金5 083 -0 屈服強度一約 190 MPa (2 8 000 psi) 平均厚度一約45毫米(1.77英吋) 於2 7°C至- 95°C (80°F至-140°F )單位熱收縮(UTC)—約 0.256%或2.56毫米/米(2.56\10_3英吋/英吋) 此實施例中鋁之選擇使得熱膨脹係數與碳包覆層 (UTC<0.02%)實質不配合。因此,較佳複合材料系統係選 自將不同包覆層層積物調整至不同CTE値,自內界面自 包覆層之外表面產生CTE梯度的組合。 再參照圖2A至圖2C,本發明四球形容器24裝於船 22上之備擇實施例,承載約200,000立方米(7062891立 方英呎)之PLNG產物,發現下列符合船及船貨要求、及 前述之襯墊功能性要求之襯墊幾何參數: 直徑一約46米(150.9英呎) 襯墊材料一INVAR-36(鐵與36%鎳之合金) 屈服強度一約 23 6.7 MPa (34·8 ksi) 極限強度一約 43 2.7 MPa (63.6 ksi) 平均厚度一約3 5毫米(1·38英吋) 於 27°C 至-162°C (8 0°F 至- 2 60 °F )單位熱收縮(UTC) — 約0.03%或0.3毫米/米(3.0x1 (Γ4英吋/英吋) 此備擇實施例係針對最小CTE不配合度係用基本材 料系統諸如前述碳-纖維-環氧樹脂系統設計。 -27- 1281011 (23) 另一備擇實施例中,發現下列符合船及船貨要求、及 前述之襯墊功能性要求之襯墊幾何參數: 直徑一約46米(150.9英呎) 襯塾材料一本發明所討論之局屈服強度鋼材 屈服強度一約 120000 psi (816 MPa) 平均厚度一約25.4毫米(1英吋) 於27°C至_95°C (80°F至-140°F )單位熱收縮(UTC)—約 0.1 2 8°/。或 1.28 毫米/米(1.28x1 0·3 英吋/英吋) 此備擇實施例使襯墊中具有較高之殘留壓縮預應力, 以補償該襯墊與該碳包覆層之間的熱收縮。 此實施例之備擇幾何形狀係爲優於球形之具有測地-等張(geodesic-isotensoid)半球的圓柱體。測地-等張 (geodesic-isotensoid)輪廓係爲半球輪廓,其中纖絲放置 於測地路徑上,使得該纖絲在負載壓力時於整體長度上皆 具有均勻張力。該測地路徑係爲兩點在表面上的最短距離 。結果,此幾何形狀使得纖維需求較球形結構降低(約低 3 0%)。此外,該測地-等張(g e 〇 d e s i c - i s 〇 t e n s 〇 i d)半球圓柱 體係爲空間利用效率高於球體的形狀。現在參照圖4,連 接於相對短圓柱形部分4 5而具有測地-等張(g e 〇 d e s i c -isotensoid)半球41之容器40係包含自持性襯墊43及複 合材料包覆層42。容器40可具有噴嘴44。現在參照圖3 ,具有扁圓球體幾何形狀之容器30係包含自持性襯墊33 及複合材料包覆層32。容器30可具有噴嘴34。 本.發明使用於P L N G之複合材料容納系統的優點包括 1281011 (24) 下列者。船設計可針對PLNG容器之幾何形狀及大尺寸最 佳化。本發明複合材料容納系統可針對PLNG輸送之獨特 大尺寸製造,即提供纖絲捲繞製造方法所使用之自持性結 構。而且,該系統於低溫條件下行使功能,因爲襯墊與複 合材料包覆層材料之間的CTE差値係適當地配合。 襯墊鋼及焊接實施例 如美國專利第60662 1 2號(及對應之國際公告編號 WO 99/3267 1 )所述,提供一種製備超高強度、雙相鋼板的 方法,該鋼板具有顯微結構,且包含約1 0體積%至約4 0 體積%之第一相,其實質爲100體積%(即實質純或”基本 上”)鐵酸鹽,及約60體積%至約90體積。/〇之第二相,其 主要爲細顆粒板條馬氏體(lath martensite)、細顆粒下貝 氏體(lower bainite)、或其混合物,其中該方法係包括下 列步驟:(a)將鋼錠加熱至再加熱溫度,其高至足以(i)實 質上將該鋼錠均勻化,(Π)實質溶解所有在鋼錠中之鈮與 釩的碳化物及碳氮化物,及(iii)於該鋼錠中建立起始之沃 斯田體(austenite)晶粒;(b)於沃斯田體再結晶之第一溫度 範圍內,於一或多個熱軋程序中,將該鋼錠縮小形成鋼板 ;(Ο於低於約Tnr溫度且高於Ar3轉化溫度間之第二溫度 範圍內,於一或多個熱軋通程中,進一步縮小該鋼板; (d)於低於約Ar3轉化溫度且高於約Ar!轉化溫度間之第三 溫度範圍內(即,中間臨界溫度範圍(intercritical temperature range)),於一或多個熱軋程序中,進一步縮 1281011 (25) 小該鋼板;(e)於每秒約l〇°C至每秒約40°C(18°F/秒至72 °F /秒)之冷卻速率下,將該鋼板驟冷至驟冷終止溫度 (Q S T),以低於約該M s轉化溫度加2 0 0 °C (3 6 0 °F )爲佳;及 (f)終止該驟冷。此鋼例之另一實施例中,Q S T以低於約 該Ms轉化溫度加10(TC (180°F )爲佳,低於約3 5 0 °C (662 °F )更佳。此鋼實例之一實施例中,該鋼板係於步驟(f)之 後,以空氣冷卻至室溫。此處理有助於該鋼板之顯微結構 轉化成約1 〇體積%至約40體積%之鐵酸鹽第一相,及約 60體積%至約9 0體積%之主要細粒板條馬氏體、細粒下 貝氏體或其混合物的第二相。(參照辭庫中Tnr溫度及Ar3 、An、及Ms轉化溫度之定義)。 爲確定環境及低溫韌性,此鋼實例中第二相之顯微結 構係主要包含細粒下貝氏體、細粒板條馬氏體、或其混合 物。較佳係實質上使第二相中之脆化成份諸如上貝氏體、 攣晶馬氏體、及MA減至最少。此鋼實例及申請專利範圍 中所使用之”主要”意指至少約50體積百分比。其餘第二 相顯微結構可包含其他細粒下貝氏體、其他細粒板條馬氏 體、或鐵酸鹽。該第二相之顯微結構以包含至少約60體 積百分比至約8 0體積百分比之細粒下貝氏體、細粒板條 馬氏體、或其混合物更佳。該第二相之顯微結構包含至少 約90體積百分比之細粒下貝氏體、細粒板條馬氏體、或 其混合物更佳。 製造此例之鋼材時,依習用方式製造鋼錠,其包含鐵 及下列合金元素,以下列重量百分比範圍爲佳:. 〇4至 -30- 1281011 (26) 〇·12 碳(C),0·04 至 0.07C 更佳;0·5 至 2.5 錳(Μη),1·〇 至1·8 Μη更佳;1.0至3·0鎳(Ni),以1·5至2.5 Ν更佳 ;0.02 至 0·1 鈮(Nb),0.02 至 0.05 Nb 更佳;0.00 8 至 0.03 鈦(Ti),0.01 至 0.02Ti 更佳;0.001 至 0.05 鋁(A1), 0.005 至 0.03A1 更佳;及 0.002 至 0.005 氮(N),0.002 至 0.003 N更佳。有時添加鉻(Cr)於該鋼材,以最高達約1.0 重量%爲佳,約0.2重量%至約0.6重量%更佳。有時添加 鉬(Mo)於該鋼材,以最高達約0.8重量%爲佳,約0.1重 量%至約0.3重量%更佳。有時添加矽(Si)於該鋼材,以最 高達約0.5重量%爲佳,約0.01重量%至約0.5重量%更 佳,而約0.05重量%至約0.1重量%又更佳。有時添加銅 (Cu)於該鋼材,以約0.1重量%至約1.0重量%爲佳,約 0.2重量%至約0.4重量%範圍內更佳。有時添加硼(B)於 該鋼材中,以最高達約0.0020重量%爲佳,而約0.0006 重量%至約0.0010重量%更佳。該鋼材較佳係含有至少約 1重量%之鎳。若期望改善焊接後之性能,則該鋼材之鎳 含量可增加至約3重量%以上。預期每添加1重量%之鎳 ,則將該鋼材之DBTT降低約l〇°C (18°F)。鎳含量以低於 9重量%爲佳,低於約6重量%更佳。鎳含量較佳係經最 小化,以將該鋼材之成本降至最低。若鎳含量增加至約3 重量%以上,則錳含量可降低至約〇·5重量%以下,至0·0 重量%。因此,廣義上來說,以最高達約2 · 5重量%之錳 爲佳。 此外,該鋼材中之殘留物以實質最小化爲佳。碟(P) -31 - 1281011 (27) 含量以低於約0.01重量%爲佳。硫(S)含量以低於約0.004 重量%爲佳。氧(0)含量以低於約0.002重量%爲佳。 稍詳述之,此鋼材實例之鋼材係藉由形成具有所需組 成之鋼錠;將該鋼錠加熱至由約9 5 5 °C至約1 0 6 5 °C (1 7 5 0 °F至1 95 0 °F )之溫度;該鋼錠於沃斯田體再結晶之第一溫 度車E圍內(即局於約該T n r溫度)分一或多程進行熱軋,縮 減約3 0百分比至約7 0百分比,以形成鋼板,該鋼板於低 於約該Tnr溫度且高於約Ar3轉化溫度之第二溫度範圍內 ,分一或多程再進行熱軋,縮減約4 0百分比至約8 0百分 比,且於低於約Ar3轉化溫度且高於約Ar!轉化溫度之中 間臨界溫度範圍內,分一或多程使該鋼板進行終段軋壓, 使之縮減約1 5百分比至約5 0百分比。經軋壓之鋼板隨之 於約每秒1 0 °C至約每秒4 0 °C (1 8 °F /秒至7 2 T /秒)之冷卻 速率下驟冷至適當之驟冷終止溫度(QST),以低於約該Ms 轉化溫度加200 °C (3 60 °F )爲佳此時終止驟冷。此實例之另 一實施例中,該QST以低於約該Ms轉化溫度加l〇〇°C (1 80°F )爲佳,低於約3 5 0 °C (662 °F )更佳。此鋼實例之一 實施例中,該鋼板係於終止驟冷之後,以空氣冷卻至室溫 〇 如熟習此項技術者已知,本發明所使用之”厚度縮減 百分比”意指該鋼錠或鋼板於所稱縮減之前的厚度縮減百 分比。在僅供說明而不限制此實例之情況下,約2 5.4厘 米(1 0英吋)厚度之鋼錠可於第一溫度範圍內縮減約 5 0%(50百分比縮減),成爲約12.7厘米(5英吋)厚度,之 1281011 (28) 後於第二溫度範圍內縮減約80%(80百分比縮減),成爲約 2.5厘米(1英吋)厚度。再次出示僅供說明而不限制此實例 之情況,約25·4厘米(10英吋)厚度之鋼錠可於第一溫度 範圍內縮減約30% (30百分比縮減),成爲約17.8厘米(7 英吋)厚度,之後於第二溫度範圍內縮減約8 0 % (8 0百分比 縮減),成爲約3.6厘米(1 .4英吋)厚度,之後於第三溫度 範圍內縮減約30%(30百分比縮減),成爲約2.5厘米(1英 吋)厚度。本發明所使用之”鋼錠”意指具有任何尺寸之鋼 片。 就此例示鋼材而言,如熟習此項技術者已知,該鋼錠 較佳係藉適當之方式再加熱,以將實質整體鋼錠之溫度… 以整體鋼錠爲佳…提高至所需之再加熱溫度,例如將該鋼 錠放置於爐具中歷經一段時間。應使用之特定再加熱溫度 可由熟習此項技術者藉著實驗或使用適當之模型計算而輕 易決定。此外,將實質整體鋼錠之溫度…以整體鋼錠爲 佳…提高至所需之再加熱溫度所需之爐具溫度及再加熱時 間可由熟習此項技術者參照標準工業刊物而輕易決定。 就此例示鋼材而言,如熟習此項技術者已知,界定介 於再結晶範圍與非再結晶範圍之間的界限的溫度Tnr溫度 係視該鋼材之化學性質尤其是軋壓前之再加熱溫度、碳濃 度、鈮濃度及於軋壓過程中所出現之縮減量而定。熟習此 項技術者可藉實驗或模擬計算(model calculation)決定各 鋼材組成物之溫度。相同地,本發明所使用之An、Ar2 及Ms轉化溫度可由熟習此項技術者藉著實驗或模擬計算 -33· 1281011 (29) 而決定。 就此鋼材實例而言,如熟習此項技術者已知,除了施 加於實質整體鋼錠之再加熱溫度之外,描述本實例處理方 法中所描述之後續溫度係爲在鋼材表面上測量之溫度。該 鋼材之表面溫度可使用例如光學高溫計測量,或使用適於 測量鋼材之表面溫度的任何其他裝置測量。本發明所述之 冷卻速率係位於中心者,或實質上位於中心者,或爲鋼板 厚度者;而驟冷終止溫度(QST)係爲在驟冷終止之後,因 爲鋼板中間厚度所傳導之熱,而於鋼板表面所達之最高… 或實質最高--溫度。例如,在此實例鋼材組成物的實驗加 熱處理期間,熱偶放置於鋼板厚度中心,或實質中心,以 測量中心溫度,而表面溫度係使用光學高溫計測量。導出 中心溫度與表面溫度之間的關係,以使用於後續相同…或 實質相同…鋼材組成物處理過程,以經由直接測量表面溫 度決定中心溫度。而且,達到所需加速冷卻速率所需之驟 冷流體溫度及流速可由熟習此項技術者參照標準工業刊物 而決定。 熟習此項技術者具有使用本發明所提供之資訊的必要 知識及技巧,可製造具有適當之高強度及韌性的超高強度 、低合金鋼板,以使用於構建本發明襯墊。 熟習此項技術者具有使用本發明所提供之資訊的必要 知識及技巧,可製造與本發明實施例所製之鋼板厚度比較 之下具有經修飾厚度之超高強度、低合金鋼板,同時仍製 得使用於構建本發明襯墊之具有適當之高強度及適當之低 -34- 1281011 (30) 溫韌性的鋼板。可有或稍後將發展其他適當之鋼材。所有 鋼材皆包括於本發明範圍內。 使用雙相鋼材以構建本發明包覆複合材料之容器襯墊 時,該雙相鋼材較佳處理方式係鋼材保持於中間臨界溫度 範圍以產生該雙相結構之時段係處於該加速冷卻或驟冷步 驟之前。較佳處理係該雙相結構係於在該Ar3轉化溫度至 約該Ar 1轉化溫度間冷卻該鋼材期間形成。用於構成本發 明襯墊之鋼材的另一優點係在完成加速冷卻或驟冷步驟時 ,該鋼材具有大於 690 MPa (100 ksi)之屈服強度及低於 約-73°C(-100°F)之DBTT,即不使用任何需要再加熱該鋼 材的附加處理,諸如回火。更佳情況係該鋼材在完成驟冷 或冷卻步驟時之屈服強度大於約690 MPa (100 ksi)。 爲了將鋼材接合於本發明襯墊上,需要適當之鋼板接 合方法。可針對本發明提供適當之強度及韌性之任何接合 方法皆適用。使用適於提供適當之強度及破裂韌度以容納 或運輸流體之焊接方法,以構建本發明襯墊。該焊接方法 較佳係包括適當之消耗性焊絲、適當之消耗性氣體、適當 之焊接程序、及適當之焊接方法。例如,氣體保護金屬極 電弧焊接(GMAW)及惰性氣體保護鎢極電弧焊接(TIG)…兩 者皆爲製鋼工業所熟知一皆可用於接合該鋼板,其先決條 件爲使用適當之可燃性焊絲-氣體組合物。 第一個例示焊接方法中,使用氣體保護金屬極電弧焊 接(GMAW)產生焊接金屬化學物質,其包含鐵及約0.07重 量%碳、約2 · 0 5重量%猛、約0 · 3 2重量%砂、約2.2 0重 -35- 1281011 (31) 量°/〇鎳、約0.45重量%鉻、約0.56重量%鉬、低於約no P p m碟、及低於約5 0 p p m硫。該焊接係於鋼材上進行, 諸如任何前述鋼材,使用以氬爲主而含有低於約1重量% 之氧的保護氣體。該焊接熱輸入係爲約0.3仟焦耳/毫米 至約1.5仟焦耳/毫米(7.6仟焦耳/英吋至38仟焦耳/英吋) 範圍內。藉此方法進行之焊接提供一焊接結構(參照辭庫) ,具有大於900 MPa (130 ksi)之抗張強度,以大於約930 MPa(135 ksi)爲佳,大於約965 MPa (140 ksi)更佳,而至 少約1 000 MPa (145 ksi)又更佳。此外,藉此方法焊接提 供DBTT低於約-73°C(-100°F)之焊接金屬,以低於約-96 °C(-140°F)爲佳,低於約·1〇6°〇:(-160°Ρ)更佳,而低於約 -1 15t: (“75°F )又更佳。 另一例示焊接方法中,使用GMAW方法產生焊接金 屬化學物質,其包含鐵及約0.10重量%碳(以低於約0.10 重量%碳爲佳,由約〇·〇7至約〇·〇8重量%碳更佳)、約 1 .60重量%錳、約 0.25重量%矽、約1.87重量%鎳、約 〇·87重量%鉻、約0.51重量%鉬、低於約75 ppm磷、及 低於約100 ppm硫。該焊接熱輸入係爲約0.3仟焦耳/毫 米至約1.5仟焦耳/毫米(7.6仟焦耳/英吋至38仟焦耳/英 吋)範圍內,且使用約1〇〇 °C (212 °F )之預熱。該焊接係於 鋼材上進行,諸如任何前述鋼材,使用以氬爲主而含有低 於約1重量%之氧的保護氣體。藉此方法進行之焊接提供 一焊接結構,具有大於900 MPa (130 ksi)之抗張強度,以 大於約 93 0 MPa(135 ksi)爲佳,大於約 965 MPa (140 ksi) -36· 1281011 (32) 更佳,而至少約1 000 MPa (145 ksi)又更佳。此外,藉此 方法焊接提供DBTT低於約- 73°C (-l〇〇°F )之焊接金屬,以 低於約-96°C(-140°F)爲佳,低於約-106°C(-160°F)更佳, 而低於約-115°(:(-175°?)又更佳。 另一例示焊接方法中,使用惰性氣體保護鎢極電弧焊 接(TIG)方法產生焊接金屬化學物質,其包含鐵及約0.07 重量%碳(以低於約0.07重量%碳爲佳)、約1.80重量%錳 、約0.2重量%矽、約4.00重量%鎳、約0.5重量%鉻、 約0.40重量%鉬、約0.02重量%銅、約0.02重量。/〇鋁、 約0.010重量%鈦、約0.015重量%銷(Z〇、低於約50 ppm 磷、及低於約30 ppm硫。該焊接熱輸入係爲約0.3仟焦 耳/毫米至約1.5仟焦耳/毫米(7.6仟焦耳/英吋至38仟焦 耳/英吋)範圍內,且使用約10(TC (212 °F )之預熱。該焊接 係於鋼材上進行,諸如任何前述鋼材,使用以氬爲主而含 有低於約1重量%之氧的保護氣體。藉此方法進行之焊接 提供一焊接結構,具有大於900 MPa (130 ksi)之抗張強度 ,以大於約93 0 MPa(135 ksi)爲佳,大於約965 MPa (140 k s i)更佳,而至少約 1 〇 〇 〇 Μ P a (1 4 5 k s i)又更佳。此外, 藉此方法焊接提供DBTT低於約- 73°C (-100°F )之焊接金屬 ,以低於約-96t:(-140°F)爲佳,低於約·106Τ:(-160°Ρ)更 佳,而低於約-1 15°C (-175°F )又更佳。 可使用GMAW或TIG焊接方法製得實施例所述之焊 接金屬化學組成。然而,預期該TIG焊接在與GMAW焊 接比較之下’具有較低之雜質含量及較高度精煉之顯微結 -37- 1281011 (33) 構,因此改善低溫韌性。 熟習此項技術者具有使用本發明所提供之資訊的必要 知識及技巧,焊接超高強度、低合金鋼板,產生具有適當 之高強度及破裂韌性的接點,以製造本發明襯墊。可有或 稍後將發展其他適當之接合或焊接方法。所有接合或焊接 方法皆包括於本發明範圍內。 如熟習此項技術者已知,在設計自焊接鋼材構成而包 覆複合材料之用以儲存且輸送加壓低溫流體諸如PLNG的 容器襯墊時列入考慮之操作條件係特別包括操作壓力及溫 度,及易施加於鋼材及焊接結構(參照辭庫)之附加應力。 標準破裂力學測量諸如⑴臨界應力強度因子(KIC),此係 平面應變破裂韌性之量度,及(ii)裂紋尖端張開位移 (CTOD),其可用於量度彈性-塑性破裂靭性--兩者皆爲熟 習此項技術者所熟知…可用於量度該鋼材及焊接結構之破 裂韌度。可使用一般鋼材結構設計可接受之標準,例如 B SI 公告 ”Guidance on methods for assessing the acceptability of flaws in fusion welded structures”--通稱 爲”PD 6493: 1 99 1 ”所列者,以基於該鋼材及焊接結構之破 裂韌度(包括HAZ)及作用於襯墊上之應力,決定襯墊最大 容許瑕疵尺寸。熟習此項技術者可發展破裂控制程序,以 經由(i)適當之襯墊設計,使施加之應力最小化,(Π)適當 之製造品質控制,以使缺陷最小化,(iii)施加於襯墊之循 環負荷及壓力的適當控制,及(W)適當之檢視程序,以可 信地偵測該襯墊中之瑕疵及缺陷,而減少破裂開始發生。 -38- 1281011 (34) 本發明系統之較佳設計哲學係爲”損壞前洩漏”,如熟習此 項技術者已知。此等考慮於本發明中通稱爲”破裂動物之 已知原理”。 下列係將此等已知破裂力學原理應用於在特定瑕疵長 度下計算瑕疵深度的非限制實施例,以於破裂控制計畫中 防止本發明襯墊中開始產生破裂。 圖8B說明具有瑕疵長度315及瑕疵深度310之瑕疵 。使用PD6493以基於下列針對本發明壓力器皿或襯墊之 設計條件,計算圖8A(橫座標3 02表示CTOD破裂韌度, 毫米,而縱座標301表示臨界瑕疵深度,毫米),所示之 臨界瑕疵尺寸繪圖3 00的値: 器皿直徑:4.57米(15英呎) 器皿壁厚:25.4毫米(1.00英吋) 設計壓力:3445 kPa (500 psi) 容許周向應力·· 333 MPa (48·3 ksi) 就此實例而言,假設表面瑕疵長度100毫米(4英吋) ,例如,位於線焊中之軸向瑕疵。現在參照圖8A,圖 300顯示當殘留應力爲15百分比屈服應力(線303)、50百 分比屈服應力(線304)、及100百分比屈服應力(線3 0 5 )下 之臨界瑕疵深度値,以CTOD破裂韌度及殘留應力之函數 表示。殘留應力會因製造及焊接而產生;且PD 64 93建議 焊接(包括焊接HAZ)中使用100百分比屈服應力之殘留應 力値,除非使用技術諸如焊接後熱處理(PWHT)或機械消 除應力法來消除焊接物中之應力。 -39- 1281011 (35) 基於該鋼材於最低作用溫度下的CTOD破裂韌度,該 襯墊製造可經調整以降低殘留應力,且可進行檢視程序( 同時進行起始檢視及使用中檢視),以針對於臨界瑕疵尺 寸偵測對照用瑕疵。此實施例中,若該鋼材於最低使用溫 度下具有0.025毫米之CTOD韌性(使用實驗室試樣測量) ,且殘留應力降低至該鋼材屈服強度之1 5百分比,則臨 界瑕疵深度之値約爲4毫米(參照圖8 A中之點3 2 0)。根 據相同計算方法,如熟習此項技術者所熟知,臨界瑕疵深 度可針對各種瑕疵長度及各種瑕疵幾何形狀決定。使用此 種資訊,可發展品質控制程序及檢視程序(技術、可偵測 瑕疵尺寸、頻率),以確定在達到臨界瑕疵深度之前或在 施加設計負荷之前,先測得且補救瑕疵。基於CVN、KIC 及CTOD破裂韌性之間的公開實驗關係,該0.025毫米 CTOD韌性通常與約37焦耳之CVN値有關。此實施例不 限制本發明。 就需要鋼材彎曲之襯墊而言,例如成爲圓柱形,該鋼 材較佳係於環境溫度下彎曲成所需形狀,以避免損及該鋼 材之優越低溫韌性。若該鋼材需加熱以於彎曲後達到所需 形狀,則該鋼材以加熱至不高於約600 °C(1112°F)之溫度 爲佳,以保留前述鋼材顯微結構之優勢。 雖然本發明極適於儲存及輸送PLNG,但其不限於此 ;本發明適於儲存及輸送任何流體,包括低溫流體、加壓 流體、及低溫、加壓流體。此外,雖以針對一或多個較佳 實施例描述本發明,但已知可在不偏離本發明範圍之下進 -40- 1281011 (36) 行其他修飾,如以下申請專利範圍所列示。 辭庫75 90 kPa (1100 psia) pressure and a temperature of about -123 ° C (-190 ° F) to about -62 ° C (-8 0 ° F), the composite material contains fibers selected from the following (i Carbon '(ii) glass' (iii) kevlar, (iv) aromatic polyamine, 1281011 (14) and (v) ultra high molecular weight polyethylene. In another embodiment of the method, the at least one container comprises (a) a self-sustaining liner made of a material consisting essentially of steel having a yield strength of at least about 690 MPa (100 ksi) and a substrate and The ductile-brittle transition temperature in the heated zone after welding is less than about -62 °C (-80 °F), and provides a substantially impermeable barrier to the pressurized fluid; and (b) a carrier vessel, with the self-sustaining The liner is made from a composite material and is adapted to withstand a pressure of from about 1 03 5 kPa (150 psia) to about 7590 kPa (1100 psia) and about -123° (: (-190°? ) to a temperature of about -62° (: (-80 °F), the composite material comprises fibers selected from the group consisting of (i) carbon, (Π) glass '(iii) kevlar, (iv Aromatic polyamines, and (v) ultrahigh molecular weight polyethylene. Unlike the conventional use of non-loaded liners, the container of the present invention is designed to use a self-sustaining metal liner coated with a low temperature resin. Performance Composite Fiber. The present invention is directed to a liner, which is self-sustaining, and means that its structural integrity can be maintained. Its own weight. Once the coating is applied, the composite provides additional buckling resistance to the container. For example, reference is made to Figure 6 which has a transverse coordinate of 6 inches in millimeters and a pound per square inch. The number indicates the ordinate of the systolic pressure ordinate 61, the line 62 indicates the non-critical pressure line 'line 6 3 indicates the contraction pressure of the liner having a diameter of 1 cm, and the line 6 4 indicates the diameter of 2 〇 (6 5 · 6 inches) of the shrinkage pressure of the liner' and line 65 represents the shrinkage pressure of the liner of 40 meters (131.2 inches) in diameter. Other criteria besides the shrinkage pressure can be used to determine whether the liner of the container is self-sustaining, as It is well known to those skilled in the art. The present invention is directed to composite materials or fibers, which have high performance, meaning that the tensile strength is greater than about -19 - 1281011 (15) 340 1 MPa (500 ksi) and the modulus is greater than about 1 3 6054 MPa (20 million pounds per square inch (msi)). An embodiment includes a basic LNG spherical tank coated with a high performance composite to provide the structural integrity required for PLNG containment. The advantages and characteristics are more clearly described below. The liner itself provides primary structural support for fiber tension as it is wound onto the liner. The fibers wound on the liner contribute to the support force. The liner can withstand portions of the load contained in the container. The load of the pressurized, cryogenic fluid. As is well known to those skilled in the art, design details such as the thickness of the liner, or the percentage of load carried by the liner, are based on the inclusion of a liner and a composite coating by those skilled in the art. The materials are determined according to other factors well known to those skilled in the art. Secondly, several design studies are provided to address the difference in CTE between the metal liner and the composite. In one embodiment, the CTE difference is the use of an intermediate matrix-fiber material index that has a CTE that is substantially the same as the liner CTE of the liner interface, the further away from the liner, the lower the JCTE. In one embodiment, the outermost cladding layer consists essentially of carbon fibers for improving the latent properties or consisting essentially of a material that provides the latent properties as carbon fibers. The matrix-fiber material design comprises an in-layer hybrid fiber mixture in which carbon and glass fibers are mixed (or fiber bundles). This has the added advantage of achieving good composite compressibility. The changes in this hybrid matter are mixed in layers to use alternating layers of different fibers. The third variation includes different resin ratios of the laminate: the laminate adjacent to the liner has a resin ratio that is higher than the laminate farther from the liner, and the resin that is furthest from the laminate of the liner The proportional ratio gradually decreases as the distance from the pad increases by 1281011 (16). The resin is particularly tailored to the adjusted CTE properties to enhance the properties of the layers of the composite or laminate. If an aluminum liner is used, this study confirms that there is a relatively large difference in CTE between aluminum and carbon fiber (which is advantageous for this design due to better creep properties) and a relatively small difference between aluminum and glass fibers. The term "latent change" as used in the present invention means a time-dependent strain caused by stress. In another embodiment, the self-sustaining liner is designed to withstand the critical buckling load of the application. As a result, the interface between the metal liner and the composite cladding remains unattached. This is different from conventional padded composite container designs in which the non-loaded liner is attached to the composite cladding using an adhesive that can carry the interfacial shear produced by the application; The coating separates and the liner is less damaged. In another embodiment, the outermost cladding layer consists essentially of carbon fibers to improve creep properties or materials that provide creep properties similar to carbon fibers. An intermediate layer mainly composed of glass fibers is placed between the outermost carbon fiber clad layer and a liner made of aluminum which can be used for low temperature. The self-tightening method is used to provide residual compressive pre-stress in the liner to compensate for the differential heat shrinkage of the system. When the glass fiber intermediate layer is not used, the residual compressive pre-stress is insufficient to compensate for the much larger difference in shrinkage between aluminum and carbon. The following data for a spherical pressure vessel using aluminum 5 083 -0 illustrates this point. The interface carrying the 34 kP a (5 ksi) tension develops around the aluminum and carbon fiber composite when the pressure vessel is cooled to -95 t (-140 °F). This occurs after a self-tightening pressure of 6.78 MPa (850 psig) and subsequent 5. 1 MPa (75 0 psig) of the insured pressure, both at room temperature. Correspond to the release of self-insurance pressure -21 - 1281011 (17) The load bearing pressure is 3 40 kPa (50 psig) compression. The glass determines that the interface is positively loaded to prevent cracking of the bond wires. The low yield strength of aluminum limits the residual compressive prestress induced in the liner after the self-tightening process. In another embodiment of the invention, the outermost cladding layer consists essentially of carbon fibers to improve creep properties, or materials that provide creep properties like carbon fibers. The liner uses a material with high yield strength to induce higher residual compressive prestress. This higher pre-stress substantially compensates for the differential shrinkage between the liner and the carbon, and substantially no intermediate material, such as fiberglass or adhesive, is required between the liner and the carbon composite. In addition to high yield strength, the material needs to have adequate low temperature toughness. The high yield strength material preferably has a yield strength of at least about 690 MPa (100 ksi) on the substrate and the heated zone after welding ("HAZ"), and a ductile-brittleness of less than about -62 ° C (-80 T). Transition temperature ("DBTT"). Exemplary materials that meet the yield strength and BDTT requirements are discussed in International Publication No. WO 99/32672, WO 00/3 93 52, WO 99/32670, WO 00/40764, WO 99/3267 1, WO 00/3 7689, and WO 99/95 3 3 5 and U.S. Patent Nos. 625 1 1 98, 6254698, 60662 12, 6 1 593 1 2 and 62 64 760. A welding technique that can be used to join the steel is discussed in International Publication No. WO 0 1/63 974, WO 99/05 3 3 5, and WO 00/56498, and U.S. Patent Nos. 6,114,656 and 6,336, 583. Other suitable steel and welding techniques may exist or develop later. All steel and welding techniques are included within the scope of the invention. Non-limiting liner steel and welding examples are provided at the end of the Detailed Description of the Invention. -22- 1281011 (18) The design provided has several advantages over the steel-based PLNG containment system, including: (i) simplified manufacturing method; (ii) reduced weight of the containment system, designed for transport vessels There is a positive impact; (iH) product piping requirements are greatly simplified; (iv) unloading flow chart is simplified; and (v) insulation requirements are reduced. [Embodiment] Composite Coating Layer The composite cladding layer of the container of the present invention preferably provides a main structural support for the operation load. The composite coating is preferably a material system comprising high performance fibers in a resin matrix that can be used at low temperatures. As used herein, "low temperature," means any temperature of about _62 ° C (-80 T ) and colder. An example of such a resin is CTD 525 epoxy low temperature resin. Two types of material systems have been designed in the present invention. One type of material system consists of (i) high performance fibers, preferably selected from the following fibers (carbon, glass, kevlar, aromatic polyamine, UHMWP); and (Π) thermosetting resins. (such as CTD-525 epoxy low temperature resin). One embodiment uses high performance carbon fiber such as TORAY T-700, GRAFIL 34-600 or ZOTTEC PANEX 35 for better creep properties. This first type of material system It is characterized by a fixed CTE 値. For example, the average CTE 测量 measured for carbon/epoxy laminates at room temperature and -73 t (-100 °F) is l.lxl·7 m/m/K (0·19χ10·6 in/in/°F). This crucible is generally combined with several metal liners, especially aluminum and the high yield strength steel discussed in the present invention, ie having at least about 690 MPa (100 - 23- 1281011 (19) ksi) Yield strength of steel. The second type of material system is characterized by an adjustable CTE値 and contains fibers ( Combining different fibers, such as glass and carbon, with various resin compositions. The resin composition may comprise a resin having substantial purity, and an additive designed to change the CTE of the resin. By judiciously, parameters such as fiber ratio, resin fraction And optimizing the content of the additive to obtain a preferred CTE. The representative measurement of the CTE system is - for example, does not limit the aluminum 7.2 χ 1 (Γ6 m/m/K (13xl0·6 in/in/°F) of the present invention, Pure resin 18·8χ1 (Γ6 m/m/K (33·9χ10·6 in/in/°F), and carbon 1 · 1 x 1 0·7 m/m/K (0.1 9x 1 Ο·6 in/ InTF). The optimization method required is well known to those skilled in the art, based on the desired performance parameters of the container to be constructed. Furthermore, the different laminates of the coating are adjusted to different CTEs, resulting in CTE self. The pad interface has a grade to the outer surface of the cladding. This grade is designed to achieve acceptable interlaminar stress. This acceptable factor can be determined by analytical techniques such as detailed finite element analysis (FEA analysis). As is well known to those skilled in the art. A spacer material having any CTE characteristics can be used with the second type of material. Conversely, the fixed CTE値 characteristics of the first type of material limit its use to liners with closely fitting CTEs, such as liners made by INVAR. The average CTE tantalum of INVAR has the same size as carbon, 5.0·χ1 ( Γ7 in/in/K is more than l.lxlO·7 in/in/K (0.9xl (T6 in/in/. !? Than 〇·19χ10_6 irWin/°F ). Another aspect of the invention is to use an intermediate material having a high strain capacity at the interface between the liner and the material system of the first type, that is, the strain energy absorption capacity is greater than about 34 joules per square meter (3 square feet per square inch). 0χ10·3 Btu). -24- 1281011 (20) Metal Liner The metal liner of the container of the present invention preferably has three main functions: (i) providing an impermeable barrier to the contained fluid; (ii) providing fiber during winding The primary structural support force required for tension; and (iii) providing at least partial structural support for the operational load. In addition, the liner provides at least partial structural support for operating loads and applied loads due to internal pressure of the PLNG, such as due to vessel movement. Referring to Figure 5, an embodiment of the container 5 of the present invention comprises a composite vessel 12 and a liner 10 made of a substantially impermeable material such as aluminum or a high yield strength steel as discussed herein, i.e., It has a yield strength of at least about 6 90 MPa (100 ksi) which provides a barrier to the PLNG contained in the container 5. In this embodiment, the composite vessel 12 is subjected to the structure of the tamper 5, including what the internal pressure is. The lining 10 is completely surrounded by the composite material 12 and is therefore a fully coated pressure vessel. Another example of a surrounding wrap can be designed in which the liner 10 is sized to carry the full load in the hemispherical portion. Preferably, the container 5 is protected by an outer coating 14 and is made of a material that protects the composite vessel 12 from moisture, acids, ultraviolet light and other environmentally hazardous materials. For example, without limiting the invention, the outer coating 14 can be made from polyurethane vinegar. The container 5 can also include a carrier system. For example, a reinforcing relief (not shown in Figure 5) may be provided at the bottom end of the container 5 as an interface with the support skirt (not shown in Figure 5). The design of the support skirt can have any general design' as is well known to those skilled in the art. Preferably, any additional reinforcement is provided. 1281011 (21) The relief is integrally wound into a composite vessel. This provides an important economy ^' also improves the structural strength and integrity of the interface between the support system and the container 5. A nozzle 20 is provided, preferably at the top end of the container 5, for penetration into the container 5, for example to load or remove PLNG. In one embodiment, the nozzle 20 is derived from a metal relief (not shown in Figure 5) and is disposed prior to winding the composite material comprising the composite vessel 12. The metal relief is coated with a composite material to provide a non-leakage and high strength interface to the interior of the container 5. In another embodiment, the horizontal orientation of the container of the present invention in the marine carrier 90 maximizes the volume of the cargo, while transporting The vessel 90 has a thinner hull as illustrated in Figures 7A-7C. Referring now to Figure 7B, the length of the horizontally oriented container 92 is preferably defined such that each container 92 can be supported at two points, such as points 93 and 94. With regard to the complex movement of the PLNG carrier 90, a simple two-point support system is advantageous for horizontally oriented containers 92, as is well known to those skilled in the art. As is well known to those skilled in the art, the two point support system steps the length of the container 92. When the design requires a storage capacity greater than that of a container having an allowable length of the two-point support system, a slight increase in the complexity of the support system may use a container having a longer length. As shown in Fig. 1, the container 1 of the present invention comprising a self-sustaining liner 3 and a composite coating layer 2 may have a spherical shape. The container 1 can include a nozzle 4 for penetrating into the container 1. Referring now to Figure 2A, an embodiment of a four-spherical container 24 of the present invention mounted on a vessel 22 carries about 200,000 cubic meters of PLNG product 'found below the ship and cargo requirements, and the aforementioned liner functionality - 26- 1281011 (22) Required gasket geometry: diameter of about 46 meters (150.9 inches) gasket material - aluminum alloy 5 083 -0 yield strength - about 190 MPa (2 8 000 psi) average thickness of about 45 Millimeter (1.77 inches) at 2 7 ° C to - 95 ° C (80 ° F to -140 ° F ) unit heat shrinkage (UTC) - about 0.256% or 2.56 mm / m (2.56 \ 10_3 inches / inch The choice of aluminum in this embodiment is such that the coefficient of thermal expansion and the carbon coating (UTC) <0.02%) Substantially does not match. Thus, the preferred composite system is selected from the group that adjusts the different cladding layers to different CTEs and produces a combination of CTE gradients from the outer surface of the cladding from the inner interface. Referring again to Figures 2A through 2C, an alternative embodiment of the four-ball container 24 of the present invention mounted on the vessel 22 carries about 200,000 cubic meters (7062891 cubic feet) of PLNG product and is found to meet the ship and cargo requirements, and The pad geometry required for the aforementioned pad functional requirements: diameter of about 46 meters (150.9 inches) pad material - INVAR-36 (iron and 36% nickel alloy) yield strength of about 23 6.7 MPa (34·8) Ksi) ultimate strength - about 43 2.7 MPa (63.6 ksi) average thickness of about 35 mm (1·38 inches) at 27 ° C to -162 ° C (8 0 ° F to - 2 60 ° F ) unit heat Shrinkage (UTC) - about 0.03% or 0.3 mm/m (3.0x1 (Γ4 inches/inch) This alternative embodiment is for a minimum CTE unsuitability system using a basic material system such as the aforementioned carbon-fiber-epoxy System Design -27- 1281011 (23) In another alternative embodiment, the following gasket geometry parameters meeting ship and cargo requirements and the aforementioned pad functional requirements were found: diameter of approximately 46 meters (150.9 inches) Lining material - The yield strength of the steel discussed in the present invention is about 120,000 psi (816 MPa). Approximately 25.4 mm (1 inch) at 27 ° C to _95 ° C (80 ° F to -140 ° F ) unit heat shrinkage (UTC) - about 0.1 2 8 ° /. or 1.28 mm / m (1.28x1 0·3 吋/英吋) This alternative embodiment provides a higher residual compressive pre-stress in the liner to compensate for thermal contraction between the liner and the carbon coating. The geometry is a cylinder with a geodetic-isotensoid hemisphere superior to a sphere. The geodesic-isotensoid profile is a hemispherical profile in which the filaments are placed on a geodetic path such that the fiber The wire has a uniform tension over the entire length of the load. The geodesic path is the shortest distance between the two points on the surface. As a result, this geometry results in a lower fiber requirement than the spherical structure (about 30% lower). The geodetic-isolation (ge 〇desic - is 〇tens 〇id) hemispherical cylindrical system has a space utilization efficiency higher than that of the sphere. Referring now to Figure 4, it is connected to the relatively short cylindrical portion 45 and has geodesic-isolation ( Ge 〇desic -isotensoid) hemisphere 41 container 40 contains The retaining liner 43 and the composite coating 42. The container 40 can have a nozzle 44. Referring now to Figure 3, the container 30 having the oblate spheroid geometry includes a self-sustaining liner 33 and a composite coating 32. The container 30 can have a nozzle 34. Advantages of the present invention for a composite containment system for P L N G include 1281011 (24). The boat design is optimized for the geometry and large size of the PLNG container. The composite containment system of the present invention can be manufactured for the unique large size of PLNG transport, i.e., provides a self-sustaining structure for use in the filament winding manufacturing process. Moreover, the system functions under low temperature conditions because the CTE difference between the liner and the composite cladding material is properly matched. A method of preparing an ultra-high strength, dual-phase steel sheet having a microstructure, as described in U.S. Patent No. 6,066,621 (and the corresponding International Publication No. WO 99/3267 1), which is incorporated herein by reference. And comprising from about 10% by volume to about 40% by volume of the first phase, which is substantially 100% by volume (i.e., substantially pure or "substantially") ferrite, and from about 60% to about 90 volumes. a second phase of bismuth, which is mainly a fine particle lath martensite, a lower bainite, or a mixture thereof, wherein the method comprises the following steps: (a) ingot Heating to a reheating temperature which is high enough to (i) substantially homogenize the ingot, (Π) substantially dissolve all of the niobium and vanadium carbides and carbonitrides in the ingot, and (iii) in the ingot Establishing an initial austenite grain; (b) in the first temperature range of recrystallization of the Worth field, the steel ingot is reduced to form a steel plate in one or more hot rolling processes; Further reducing the steel sheet in one or more hot rolling passes at a second temperature range below about Tnr temperature and above the Ar3 conversion temperature; (d) below about Ar3 conversion temperature and above about In the third temperature range between Ar! conversion temperatures (ie, the intercritical temperature range), in one or more hot rolling procedures, the steel plate is further reduced by 1281011 (25); (e) per Cooling speed from about 10 ° C to about 40 ° C (18 ° F / sec to 72 ° F / sec) per second At a rate, the steel plate is quenched to a quenching termination temperature (QST), preferably less than about the M s conversion temperature plus 200 ° C (360 ° F); and (f) terminating the quenching In another embodiment of this steel example, QST is preferably less than about the Ms conversion temperature plus 10 (TC (180 °F), more preferably less than about 350 ° C (662 °F). In one embodiment of the example, the steel sheet is cooled to room temperature with air after step (f). This treatment facilitates the transformation of the microstructure of the steel sheet to from about 1% by volume to about 40% by volume of ferrite. a first phase, and a second phase of from about 60% by volume to about 90% by volume of the main fine-grained lath martensite, the lower-grain bainite or a mixture thereof (refer to the Tnr temperature and Ar3, An in the dictionary) And the definition of Ms conversion temperature.) In order to determine the environmental and low temperature toughness, the microstructure of the second phase in this steel example mainly includes fine-grained bainite, fine-grained lath martensite, or a mixture thereof. The system essentially minimizes the embrittlement components in the second phase, such as upper bainite, twin martensite, and MA. This steel example and the scope of the patent application are used primarily. Means at least about 50 volume percent. The remaining second phase microstructure may comprise other fine subgranular bainite, other fine grain lath martensite, or ferrite. The microstructure of the second phase to contain at least More preferably from about 60% by volume to about 80% by volume of finely divided bainite, fine-grained lath martensite, or a mixture thereof. The microstructure of the second phase comprises at least about 90% by volume of fine particles. Bainite, fine-grained lath martensite, or a mixture thereof is preferred. When manufacturing the steel of this example, a steel ingot is prepared by the conventional method, which comprises iron and the following alloying elements, preferably in the following percentage by weight: 〇4 To -30- 1281011 (26) 〇·12 carbon (C), 0·04 to 0.07C is better; 0·5 to 2.5 manganese (Μη), 1·〇 to 1·8 Μη is better; 1.0 to 3· 0 nickel (Ni), more preferably from 1. 5 to 2.5 ;; 0.02 to 0·1 铌 (Nb), more preferably from 0.02 to 0.05 Nb; from 0.008 to 0.03 titanium (Ti), preferably from 0.01 to 0.02 Ti; To 0.05 aluminum (A1), preferably 0.005 to 0.03A1; and 0.002 to 0.005 nitrogen (N), preferably 0.002 to 0.003 N. Chromium (Cr) is sometimes added to the steel, preferably up to about 1.0% by weight, more preferably from about 0.2% by weight to about 0.6% by weight. Molybdenum (Mo) is sometimes added to the steel, preferably up to about 0.8% by weight, more preferably from about 0.1% by weight to about 0.3% by weight. Niobium (Si) is sometimes added to the steel, preferably up to about 0.5% by weight, more preferably from about 0.01% to about 0.5% by weight, still more preferably from about 0.05% to about 0.1% by weight. Copper (Cu) is sometimes added to the steel, preferably from about 0.1% by weight to about 1.0% by weight, more preferably from about 0.2% by weight to about 0.4% by weight. Boron (B) is sometimes added to the steel in an amount of up to about 0.0020% by weight, more preferably from about 0.0006% by weight to about 0.0010% by weight. Preferably, the steel material contains at least about 1% by weight nickel. If it is desired to improve the properties after welding, the nickel content of the steel can be increased to about 3% by weight or more. It is expected that the DBTT of the steel will be reduced by about 10 ° C (18 ° F) per 1% by weight of nickel added. The nickel content is preferably less than 9% by weight, more preferably less than about 6% by weight. The nickel content is preferably minimized to minimize the cost of the steel. If the nickel content is increased to about 3% by weight or more, the manganese content may be reduced to about 5% by weight or less to 0% by weight. Therefore, in a broad sense, manganese is preferably up to about 2.6 wt%. In addition, the residue in the steel is preferably substantially minimized. Disc (P) -31 - 1281011 (27) The content is preferably less than about 0.01% by weight. The sulfur (S) content is preferably less than about 0.004% by weight. The oxygen (0) content is preferably less than about 0.002% by weight. In more detail, the steel of this steel example is formed by forming a steel ingot having a desired composition; heating the ingot to a temperature of from about 195 ° C to about 1 0 6 5 ° C (1 7 5 0 ° F to 1) a temperature of 95 ° ° °; the steel ingot is hot rolled in one or more passes in the first temperature car E of the re-crystallization of the Worth field (ie, about the T nr temperature), and is reduced by about 30% to Approximately 70% to form a steel sheet which is hot rolled in one or more passes at a temperature lower than about the Tnr temperature and above about the Ar3 conversion temperature, and is reduced by about 40% to about 8 0%, and in the intermediate critical temperature range below about Ar3 conversion temperature and above about Ar! conversion temperature, the steel sheet is subjected to final rolling in one or more passes to reduce it by about 15 percentage points to about 5 0 percentage. The rolled steel sheet is then quenched to a suitable quenching temperature at a cooling rate of from about 10 ° C per second to about 40 ° C per second (1 8 ° F / sec to 7 2 T / sec). (QST), preferably less than about the Ms conversion temperature plus 200 °C (3 60 °F), at which point the quenching is terminated. In another embodiment of this embodiment, the QST is preferably less than about the Ms conversion temperature plus l 〇〇 ° C (1 80 ° F), more preferably less than about 350 ° C (662 ° F). In one embodiment of the steel, the steel sheet is cooled to room temperature by air after termination of quenching. As is known to those skilled in the art, the "thickness reduction percentage" as used herein means the steel ingot or steel sheet. The percentage reduction in thickness before the so-called reduction. In the case of illustration only and without limitation to this example, a steel ingot of approximately 2 5.4 cm (10 inches) thickness may be reduced by approximately 50% (50% reduction) to approximately 12.7 cm in the first temperature range (5 In English, the thickness of 1281011 (28) is reduced by about 80% (80% reduction) in the second temperature range to a thickness of about 2.5 cm (1 inch). Again for illustrative purposes without limiting this example, a steel ingot of approximately 25.4 cm (10 inches) thickness can be reduced by approximately 30% (30% reduction) to approximately 17.8 cm (7 inches) in the first temperature range.吋) thickness, then reduced by about 80% (80% reduction) in the second temperature range to a thickness of about 3.6 cm (1.4 inches), and then reduced by about 30% in the third temperature range (30%) Reduced) to a thickness of about 2.5 cm (1 inch). "Steel ingot" as used in the present invention means a steel sheet having any size. In the case of the exemplified steel, as is known to those skilled in the art, the ingot is preferably reheated in a suitable manner to increase the temperature of the substantially integral ingot as a whole steel ingot to the desired reheating temperature, For example, the ingot is placed in a stove for a period of time. The particular reheating temperature that should be used can be readily determined by one skilled in the art by experimentation or by using appropriate model calculations. In addition, it is preferred that the temperature of the substantially integral ingot is as a whole ingot. The temperature and reheating time required to increase the reheating temperature required can be easily determined by those skilled in the art with reference to standard industrial publications. In the case of this exemplary steel, as is known to those skilled in the art, the temperature Tnr which defines the boundary between the recrystallization range and the non-recrystallization range depends on the chemical nature of the steel, especially the reheating temperature before rolling. , carbon concentration, strontium concentration and the amount of reduction that occurs during the rolling process. Those skilled in the art can determine the temperature of each steel composition by experiment or model calculation. Similarly, the An, Ar2 and Ms conversion temperatures used in the present invention can be determined by those skilled in the art by experimental or simulation calculations - 33· 1281011 (29). For this steel example, as is known to those skilled in the art, the subsequent temperatures described in the processing methods of this example are those measured on the surface of the steel, except for the reheating temperature applied to the substantially integral steel ingot. The surface temperature of the steel can be measured using, for example, an optical pyrometer, or any other device suitable for measuring the surface temperature of the steel. The cooling rate according to the present invention is located at the center, or substantially at the center, or is the thickness of the steel sheet; and the quenching termination temperature (QST) is the heat transmitted by the intermediate thickness of the steel sheet after the quenching is terminated. And the highest on the surface of the steel plate ... or the highest - temperature. For example, during the experimental heat treatment of the steel composition of this example, the thermocouple is placed at the center of the thickness of the steel sheet, or substantially at the center, to measure the center temperature, which is measured using an optical pyrometer. The relationship between the center temperature and the surface temperature is derived for subsequent use of the same...or substantially the same...steel composition process to determine the center temperature via direct measurement of the surface temperature. Moreover, the temperature and flow rate of the quench fluid required to achieve the desired accelerated cooling rate can be determined by those skilled in the art with reference to standard industry publications. Those skilled in the art having the necessary knowledge and skill in using the information provided by the present invention can produce ultra high strength, low alloy steel sheets having suitable high strength and toughness for use in constructing the liner of the present invention. Those skilled in the art having the necessary knowledge and skill to use the information provided by the present invention can produce ultra-high strength, low alloy steel sheets having a modified thickness compared to the thickness of the steel sheets produced in the examples of the present invention, while still making A steel sheet having a suitable high strength and suitably low -34 - 1281011 (30) temperature toughness for use in constructing the gasket of the present invention. Other suitable steels may or may be developed later. All steels are included within the scope of the invention. When a duplex steel is used to construct the container liner of the coated composite of the present invention, the duplex steel is preferably treated in such a manner that the steel is maintained at an intermediate critical temperature range to produce the dual phase structure in the accelerated cooling or quenching. Before the step. Preferably, the dual phase structure is formed during the cooling of the steel between the Ar3 conversion temperature and the Ar 1 conversion temperature. Another advantage of the steel material used to form the gasket of the present invention is that the steel has a yield strength greater than 690 MPa (100 ksi) and less than about -73 ° C (-100 ° F) upon completion of the accelerated cooling or quenching step. The DBTT, that is, does not use any additional treatment that requires reheating the steel, such as tempering. More preferably, the steel has a yield strength greater than about 690 MPa (100 ksi) upon completion of the quenching or cooling step. In order to join the steel material to the liner of the present invention, a suitable steel sheet joining method is required. Any joining method that provides suitable strength and toughness to the present invention is applicable. A welding method suitable for providing suitable strength and burst toughness to contain or transport fluids is used to construct the liner of the present invention. Preferably, the welding method includes a suitable consumable welding wire, a suitable consumable gas, a suitable welding procedure, and a suitable welding method. For example, gas shielded metal arc welding (GMAW) and inert gas shielded tungsten arc welding (TIG), both of which are well known to the steel industry, can be used to join the steel sheet, with the proviso that appropriate flammable welding wire is used - Gas composition. In a first exemplary welding method, a gas metal arc welding (GMAW) is used to produce a weld metal chemistry comprising iron and about 0.07% by weight carbon, about 0.25 wt%, about 0. 32 wt%. Sand, about 2.20 weight - 35 - 1281011 (31) amount / nickel, about 0.45 weight percent chromium, about 0.56 weight percent molybdenum, less than about no P pm dish, and less than about 50 ppm sulfur. The welding is carried out on steel, such as any of the foregoing steels, using a shielding gas containing less than about 1% by weight oxygen, based primarily on argon. The weld heat input is in the range of about 0.3 仟 joules/mm to about 1.5 仟 joules/mm (7.6 仟 joules/inch to 38 仟 joules/inch). The welding by this method provides a welded structure (referred to as a dictionary) having a tensile strength greater than 900 MPa (130 ksi), preferably greater than about 930 MPa (135 ksi), and greater than about 965 MPa (140 ksi). Good, and at least about 1 000 MPa (145 ksi) is even better. In addition, welding by this method provides a weld metal having a DBTT of less than about -73 ° C (-100 ° F), preferably less than about -96 ° C (-140 ° F), less than about 1 · 6 ° ° 〇: (-160 ° Ρ) is better, and less than about -1 15 t: ("75 ° F" is even better. In another example of the welding method, the GMAW method is used to produce a weld metal chemistry comprising iron and about 0.10% by weight of carbon (preferably less than about 0.10% by weight of carbon, more preferably from about 〇·〇7 to about 〇·〇8 wt% carbon), about 1.60% by weight of manganese, about 0.25 wt% 矽, about 1.87 wt% nickel, about 87 wt% chromium, about 0.51 wt% molybdenum, less than about 75 ppm phosphorus, and less than about 100 ppm sulfur. The weld heat input is about 0.3 仟 joules/mm to about 1.5 仟. Joules/mm (7.6 仟 joules/inch to 38 仟 joules/inch) and preheating at approximately 1 °C (212 °F). The weld is made on steel, such as any of the aforementioned steels. a shielding gas containing less than about 1% by weight of oxygen, mainly argon, is used. The welding by this method provides a welded structure having a tensile strength greater than 900 MPa (130 ksi), which is greater than 93 0 MPa (135 ksi) is preferred, greater than about 965 MPa (140 ksi) -36· 1281011 (32) is better, and at least about 1 000 MPa (145 ksi) is better. In addition, this method provides welding with DBTT. Solder metals below about -73 ° C (-l 〇〇 °F), preferably below about -96 ° C (-140 ° F), below about -106 ° C (-160 ° F) Preferably, less than about -115° (: (-175°?) is better. In another exemplary welding method, an inert gas shielded tungsten arc welding (TIG) method is used to produce a weld metal chemical comprising iron and About 0.07 wt% carbon (preferably less than about 0.07 wt% carbon), about 1.80 wt% manganese, about 0.2 wt% rhodium, about 4.00 wt% nickel, about 0.5 wt% chromium, about 0.40 wt% molybdenum, about 0.02 Weight % copper, about 0.02 wt./〇 aluminum, about 0.010 wt% titanium, about 0.015 wt% pin (Z〇, less than about 50 ppm phosphorus, and less than about 30 ppm sulfur. The weld heat input is about 0.3).仟 joules/mm to about 1.5 仟 joules/mm (7.6 仟 joules/inch to 38 仟 joules/inch) and use about 10 (TC ° 212 °F) for preheating. The weld is on steel Carry out The above steel material uses a shielding gas containing argon mainly containing less than about 1% by weight of oxygen. The welding by this method provides a welded structure having a tensile strength of more than 900 MPa (130 ksi) to be greater than about 93. 0 MPa (135 ksi) is preferred, more preferably greater than about 965 MPa (140 ksi), and at least about 1 〇〇〇Μ P a (1 4 5 ksi) is preferred. In addition, welding by this method provides a weld metal having a DBTT of less than about -73 ° C (-100 ° F), preferably less than about -96 t: (-140 ° F), less than about 106 Τ: (-160 °Ρ) is better, and less than about -1 15 ° C (-175 ° F) is better. The weld metal chemistry described in the examples can be made using GMAW or TIG welding methods. However, it is expected that the TIG welding will have a lower impurity content and a higher degree of refining of the micro-junction -37-1281011 (33) compared to the GMAW welding, thus improving the low temperature toughness. Those skilled in the art have the necessary knowledge and skill to use the information provided by the present invention to weld ultra high strength, low alloy steel sheets to produce joints of suitable high strength and fracture toughness to produce the liner of the present invention. Other suitable joining or welding methods may be developed or later. All joining or welding methods are included within the scope of the invention. As is well known to those skilled in the art, the operating conditions contemplated for use in the design of self-welding steel and coated composite materials for storing and transporting pressurized cryogenic fluids such as PLNG include operating pressures and temperatures. And additional stresses that are easily applied to steel and welded structures (see lexicon). Standard fracture mechanics measurements such as (1) critical stress intensity factor (KIC), a measure of plane strain fracture toughness, and (ii) crack tip opening displacement (CTOD), which can be used to measure elastic-plastic fracture toughness - both As is well known to those skilled in the art, it can be used to measure the fracture toughness of the steel and welded structure. Acceptable standards for general steel structure design, such as those listed in the B SI Bulletin "Guidance on methods for assessing the acceptability of flaws in fusion welded structures" - commonly known as "PD 6493: 1 99 1", based on the steel And the fracture toughness of the welded structure (including HAZ) and the stress acting on the liner determine the maximum allowable crucible size of the liner. Those skilled in the art can develop a fracture control program to minimize stress applied by (i) appropriate pad design, (ie) appropriate manufacturing quality control to minimize defects, and (iii) application to the liner. Appropriate control of the cyclic loading and pressure of the mat, and (W) appropriate inspection procedures to reliably detect flaws and defects in the liner to reduce the onset of cracking. -38- 1281011 (34) The preferred design philosophy of the system of the present invention is "leakage prior to damage" as is known to those skilled in the art. Such considerations are generally referred to in the present invention as "known principles of ruptured animals." The following is a non-limiting example of applying such known principles of fracture mechanics to the calculation of the depth of the crucible at a particular crucible length to prevent cracking from occurring in the liner of the present invention in the fracture control program. Figure 8B illustrates a crucible length 315 and a crucible depth 310. Using PD6493 to calculate Figure 8A based on the following design conditions for the pressure vessel or liner of the present invention (the abscissa 323 represents CTOD fracture toughness, millimeters, and the ordinate 301 represents critical enthalpy depth, millimeters), the critical enthalpy shown Dimensional drawing 3 00 値: Vessel diameter: 4.57 m (15 ft) Vessel wall thickness: 25.4 mm (1.00 ft) Design pressure: 3445 kPa (500 psi) Allowable circumferential stress · 333 MPa (48·3 ksi For this example, it is assumed that the surface has a length of 100 mm (4 inches), for example, an axial flaw in the wire bonding. Referring now to Figure 8A, Figure 300 shows the critical enthalpy depth 当 when the residual stress is 15% yield stress (line 303), 50 percent yield stress (line 304), and 100 percent yield stress (line 305), to CTOD A function of the fracture toughness and residual stress. Residual stresses are caused by manufacturing and welding; and PD 64 93 recommends residual stresses of 100% yield stress in welding (including welding HAZ) unless techniques such as post-weld heat treatment (PWHT) or mechanical stress relief are used to eliminate welding. Stress in the material. -39- 1281011 (35) Based on the CTOD fracture toughness of the steel at the lowest operating temperature, the gasket can be adjusted to reduce residual stress and can be subjected to inspection procedures (simultaneous inspection and in-use inspection) The control sputum is detected for the critical 瑕疵 size. In this embodiment, if the steel has a CTOD toughness of 0.025 mm (measured using a laboratory sample) at the lowest use temperature and the residual stress is reduced to 15% of the yield strength of the steel, the critical enthalpy depth is about 4 mm (refer to point 3 2 0 in Figure 8 A). According to the same calculation method, as is well known to those skilled in the art, the critical enthalpy depth can be determined for various raft lengths and various 瑕疵 geometry. Using this information, quality control procedures and inspection procedures (techniques, detectable size, frequency) can be developed to determine and remediate defects before reaching critical depths or before applying design loads. Based on the open experimental relationship between CVN, KIC, and CTOD fracture toughness, the 0.025 mm CTOD toughness is typically associated with about 37 joules of CVN値. This embodiment does not limit the invention. In the case of a liner that requires steel to be bent, for example, to be cylindrical, the steel is preferably bent to a desired shape at ambient temperature to avoid impairing the superior low temperature toughness of the steel. If the steel is to be heated to achieve the desired shape after bending, the steel is preferably heated to a temperature not higher than about 600 ° C (1112 ° F) to retain the advantages of the aforementioned steel microstructure. While the present invention is highly suitable for storing and transporting PLNG, it is not limited thereto; the present invention is suitable for storing and transporting any fluid, including cryogenic fluids, pressurized fluids, and low temperature, pressurized fluids. In addition, although the invention has been described in terms of one or more preferred embodiments, it is known that other modifications can be made without departing from the scope of the invention, as set forth in the following claims. Dictionary

An轉化溫度:在冷卻期間沃斯田體完全轉化成鐵酸 鹽或轉化成鐵酸鹽加滲碳體之溫度; Αγ3轉化溫度:在冷卻期間沃斯田體開始轉化成鐵酸 鹽之溫度; CNG :壓縮天然氣; 熱膨脹或收縮係數:每單位固體體積在固定壓力下, 溫度每升高Γ時的體積增量; 潛變:由應力所致之時間-相依性應變; 低溫:約-62°C(-80°F)及更冷之任何溫度; CTE :熱膨脹或收縮係數; DBTT(延性-脆性轉變溫度):描繪結構鋼中之兩破裂 機制;溫度低於DBTT時,易因低能斷裂(脆性)破裂而損 壞,而溫度高於DBTT時,易因高能延性破裂而損壞; 高性能:就複合材料或纖維而言,意指具有高於約 3410 MPa (5 00 ksi)之抗拉強度,及大於約 1 3 6054 MPa (20 msi)之模數; INVAR:基本上由鐵及鎮組成之材料; ksi :每平方英吋之仟磅數; LNG :於大氣壓及約-162°C (-260 °F )下之液化天然氣An conversion temperature: the temperature at which the Worth field is completely converted to ferrite or converted to ferrite plus cementite during cooling; Αγ3 conversion temperature: the temperature at which the Worth field begins to convert to ferrite during cooling; CNG: compressed natural gas; thermal expansion or contraction coefficient: volume increment per unit solid volume at a fixed pressure, temperature per enthalpy; creep: time-dependent strain due to stress; low temperature: about -62° C (-80 ° F) and any colder temperature; CTE: thermal expansion or contraction coefficient; DBTT (ductile-brittle transition temperature): depict two fracture mechanisms in structural steel; when the temperature is lower than DBTT, it is easy to break due to low energy ( Brittleness is broken and damaged, and when the temperature is higher than DBTT, it is easily damaged by high energy ductile fracture; High performance: in the case of composite or fiber, it means tensile strength higher than about 3410 MPa (500 ksi), And a modulus greater than about 1 3 6054 MPa (20 msi); INVAR: a material consisting essentially of iron and town; ksi: pounds per square inch; LNG: at atmospheric pressure and about -162 ° C (- Liquefied natural gas at 260 °F

Ms轉化溫度:在冷卻期間,沃斯田體開始轉化成馬 -41 · 9 1281011 (37) 氏體之溫度; msi :每平方英吋之百萬磅數; 非承載型襯墊容器專利:美國專利第6,460,72 1號; PLNG :於約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)廣大範圍壓力及約-123°C (-190°F )至約-62°C (-80T ) 廣大範圍溫度下之加壓液化天然氣; PLNG專利:美國專利第6,085,528號; 程序組件專利:美國專利第6,212,891號; psi :每平方英吋之磅數; 自持性:在承受自身重量的情況下,可保持結構完整 性之襯墊機構; 船段係數:V/(L)(B)(T),其中V係爲船所置放之流 體體積,L係爲船垂線間之長度,B係爲船幅,且T係爲 船之吃水部分;Ms conversion temperature: During cooling, the Worth field begins to transform into the temperature of the horse -41 · 9 1281011 (37); msi: millions of pounds per square inch; non-loading liner container patent: United States Patent No. 6,460,72 1; PLNG: a wide range of pressures from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1100 psia) and about -123 ° C (-190 ° F) to about -62 ° C (-80T) Pressurized liquefied natural gas at a wide range of temperatures; PLNG patent: US Patent No. 6,085,528; Program component patent: US Patent No. 6,212,891; psi: pounds per square inch; self-sustaining: bearing its own weight In the case of a liner mechanism that maintains structural integrity; segment coefficient: V / (L) (B) (T), where V is the volume of the fluid placed by the ship, and L is the length between the vertical lines of the ship , B is the ship's width, and T is the draft of the ship;

Tnr溫度:低於此溫度時,沃斯田體無法再結晶之溫 度; 焊接結構:焊接點,包括(i)焊接金屬,(ii)受熱區 (HAZ),及(iii)在HAZ”附近”之基本金屬。被視爲HAZ之 ”附近”而爲焊接結構之一部分的基本金屬部分係視熟習此 項技術者已知之因子而定,例如(不限制於)焊接結構之寬 度、所焊接物件之尺寸、製造該物件所需之焊接結構數量 、及焊接結構間之距離。 【圖式簡單說明】 -42- 1281011 (38) 參照前述實施方式及附圖,可進一步明瞭本發明之優 點,其中: 圖1係爲本發明具有球狀幾何形狀之容器的剖面圖; 圖2A係爲本發明具有球形幾何形狀且位於PLng運 輸船體中之容器的前視剖面圖; 圖2B係爲本發明具有球形幾何形狀而具有數個容器 之PLNG運輸船體中的配置側視剖面圖; 圖2C係爲本發明具有球形幾何形狀而具有數個容器 之PLNG運輸船體中的配置上視剖面圖; 圖3係爲本發明具有扁圓類球形幾何形狀之容器的剖 面圖; 圖4係爲本發明容器之剖面圖,具有連接於相對短圓 柱形部分之測地·等張(geodesic-isotensoid)半球; 圖5說明裁切圖,本發明容器之一實施例,具有圓柱 形幾何形狀及測地-等張(g e 〇 d e s i c - i s 〇 t e n s 〇 i d)半球; 圖6係爲出示容器襯墊收縮壓力、容器襯墊厚度、及 容器襯墊直徑間之關係的圖; 圖7A係爲具有本發明圓柱形幾何形狀之水平位置容 器的PLNG運輸船體中配置的前視剖面圖; 圖7B係爲具有本發明圓柱形幾何形狀之水平位置容 器的PLNG運輸船體中配置的側視剖面圖; 圖7C係爲具有本發明圓柱形幾何形狀之水平位置容 器的PLNG運輸船體中配置的上視剖面圖; 圖8A說明在特定瑕疵長度下之臨界瑕疵深度的圖, -43- 1281011 (39) 以C TOD破裂韌度及殘留應力之函數表示;旦 圖8B係說明瑕疵之幾何形狀(長度及深度)° 雖針對較佳實施例描述本發明,但已知本發明不受限 於此。相反地,本發明係涵蓋所有可包括於本揭示之精神 及範圍內之備擇、修飾、及同等物,如所附申請專利範圍 所定義。 元件符號對照表Tnr temperature: below this temperature, the temperature at which the Worth field can no longer recrystallize; welded structure: solder joints, including (i) weld metal, (ii) heated zone (HAZ), and (iii) near HAZ" The base metal. The basic metal portion that is considered to be "near" of the HAZ and is part of the welded structure is determined by factors known to those skilled in the art, such as, without limitation, the width of the welded structure, the size of the object being welded, and the manufacture of the The number of welded structures required for the object, and the distance between the welded structures. BRIEF DESCRIPTION OF THE DRAWINGS The advantages of the present invention will be further clarified with reference to the foregoing embodiments and the accompanying drawings in which: FIG. 1 is a cross-sectional view of a container having a spherical geometry according to the present invention; Is a front cross-sectional view of a container having a spherical geometry and located in a PLng transport hull of the present invention; and FIG. 2B is a side cross-sectional view of the configuration of a PLNG transport hull having a plurality of containers having a spherical geometry of the present invention. 2C is a top cross-sectional view of a PLNG transport hull having a plurality of containers having a spherical geometry according to the present invention; and FIG. 3 is a cross-sectional view of the container having an oblate spherical geometry according to the present invention; Is a cross-sectional view of a container of the present invention having a geodesic-isotensoid hemisphere attached to a relatively short cylindrical portion; FIG. 5 illustrates a cutaway view, an embodiment of the container of the present invention having a cylindrical geometry and Geodetic-isolation (ge 〇desic - is 〇tens 〇id) hemisphere; Figure 6 shows the relationship between shrinkage pressure of the liner, the thickness of the liner of the container, and the diameter of the liner of the container. Figure 7A is a front cross-sectional view of a configuration of a PLNG transport hull having a cylindrical geometry of the present invention; Figure 7B is a PLNG transport hull having a horizontal position container of the cylindrical geometry of the present invention; Figure 7C is a top cross-sectional view of a configuration of a PLNG transport hull having a horizontally-positioned container of the cylindrical geometry of the present invention; Figure 8A illustrates a plot of critical depth at a particular length of the crucible, -43- 1281011 (39) expressed as a function of C TOD fracture toughness and residual stress; Figure 8B illustrates the geometry (length and depth) of the crucible. Although the invention has been described with respect to preferred embodiments, the invention is known. Not limited to this. Rather, the invention is to cover all alternatives, modifications, and equivalents, which are included within the spirit and scope of the disclosure. Component symbol comparison table

1,5,92,3 0,40 容器 2,32,42 複合材料.包覆層 4,20,34,44 噴嘴 3,3 3,43 自持性襯墊 10 襯墊 12 複合材料器血 14 外塗層 22 船1,5,92,3 0,40 container 2,32,42 composite. cladding 4,20,34,44 nozzle 3,3 3,43 self-sustaining gasket 10 liner 12 composite material blood 14 Coating 22 boat

2 4 球形容器 4 1 半球 9〇 輸送器m 93,94 點 •44-2 4 Spherical container 4 1 Hemisphere 9〇 Conveyor m 93,94 points •44-

Claims (1)

煩請委8明示-本案修正後是否鋩更樣實;?!:..;·: 1281011 (1) 拾、申請專利範圍 附件二A :第92106971號修正後無劃線之 中文申請專利範圍替換本民國95年2月15日呈 1 ' ~種適於儲存加壓流體之容器,其適用於約1 03 5 kPa (150 Psia)至約 759〇 kPa (11〇〇 psia)之壓力及約 _123 °C(-190°F)至約_62。0(_80卞)之溫度,該容器係包含: (a) —自持性襯墊,該自持性襯墊係針對該加壓流體 提供實質不可滲透之障壁;及 (b) —承載器皿,與該自持性襯墊接觸,該承載器皿 係自複合材料製得,且適於承受約1〇35 kPa (150 psia)至 約 7590 kPa (1 1〇〇 psia)之壓力及約- :i23°C (-19CTF )至約 -6 2°C (-8 0 °F )之溫度,且該複合材料具有一熱膨脹係數, # (i)實質上與位於該自持性襯墊界面之自持性襯墊的熱膨 脹係數相同,且(ii)其跨經該承載器皿之厚度隨著與該界 面之距離的增加而逐漸降低。 2、 如申請專利範圍第1項之容器,其中該承載器皿 具有一最外層包覆層,該包覆層基本上係由碳纖維或提供 類似碳纖維所提供之潛變性能的材料所組成。 3、 如申請專利範圍第1項之容器,其中該複合材料 係包含位於該自持性襯墊界面上之中間材料,其中該中間 材料具有適當之抗切強度或應變,以實質防止該容器於溫 度在環境溫度及約-123°c (-190T )之間變化時損壞。 4、如申請專利範圍第1項之容器,其中該自持性襯I would like to ask the Committee 8 to express it - whether the case is more correct after the amendment; ?!:..;:: 1281011 (1) Pick up, apply for patent scope Annex II A: No. 92106971 On February 15, 1995, the Republic of China was a container suitable for storing pressurized fluid, which was suitable for a pressure of about 1 03 5 kPa (150 Psia) to about 759 kPa (11 〇〇 psia) and about _123. °C (-190 °F) to a temperature of about _62. 0 (_80 卞), the container comprises: (a) - a self-sustaining liner that provides substantial impermeability to the pressurized fluid a barrier rib; and (b) a carrier vessel in contact with the self-sustaining liner, the carrier vessel being fabricated from a composite material and adapted to withstand from about 1 〇 35 kPa (150 psia) to about 7590 kPa (1 1 〇) 〇psia) pressure and about - i23 ° C (-19 CTF ) to about -6 2 ° C (-8 0 ° F), and the composite has a coefficient of thermal expansion, # (i) substantially and located The self-sustaining pad of the self-sustaining pad interface has the same coefficient of thermal expansion, and (ii) its thickness across the carrier vessel gradually decreases as the distance from the interface increases. 2. The container of claim 1, wherein the carrier has an outermost coating layer consisting essentially of carbon fibers or a material that provides creep properties similar to those provided by carbon fibers. 3. The container of claim 1, wherein the composite material comprises an intermediate material at the interface of the self-sustaining pad, wherein the intermediate material has an appropriate shear strength or strain to substantially prevent the container from being exposed to temperature. Damaged when the ambient temperature changes between approximately -123 ° C (-190 T ). 4. The container of claim 1 of the patent scope, wherein the self-sustaining lining 1281011 (2) 墊係由基本上由鋁組成之材料製得,且該複合材料係包含 選自下列者之纖維⑴碳,(ii)玻璃,(iii)凱夫拉爾(kevlar) ,(iv)芳族聚醯胺,及(v)超高分子量聚乙烯。 5、 如申請專利範圍第〗項之容器,其中該自持性襯 墊係由基本上由鋼組成之材料製得,其屈服強度至少約 690 MPa (100 ksi),其基材及焊接後之受熱區中的延性-脆性轉變溫度低於約-62 °C (-80 °F ),且該複合材料係包含 選自下列者之纖維⑴碳,(ii)玻璃,(iii)凱夫拉爾(kevlar) ,(iv)芳族聚醯胺,及超高分子量聚乙烯。 6、 一種適於儲存加壓液化天然氣之容器,其係使用 約 1 0 3 5 kPa (150 psia)至約 7 5 9 0 kPa (1100 psia)之壓力及 約-123°C(-190°F)至約-62°C(-80°F)之溫度,該容器係包含 (a) —自持性襯墊,該自持性襯墊係針對該加壓流體 提供實質不可滲透之障壁;及 (b) -承載器皿,與該自持性襯墊接觸,該承載器皿 係自複合材料製得,且適於承受約1 03 5 kPa (150 psia)至 約 7590 kPa (1100 psia)之壓力及約·123°〇:(-190°Ρ)至約 -62°C(-80°F)之溫度,且該複合材料具有實質上與位於該 自持性襯墊界面之自持性襯墊的熱膨脹係數相同熱膨脹係 數。 7、一種製造容器之方法,該容器適用於約1 03 5 kPa (150 psia)至約 75 90 kPa (1 100 psia)之壓力及約-123 t:( -190°F)至約-62°C(-80°F)之溫度下儲存加壓流體,該方法 1281011 ........... ....... .............I _ 1丨厂:' · 」, (3) i1 ....….——,」 包括下列步驟: (a) 建構一自持性襯墊,該自持性襯墊適於針對該加 壓流體提供實質不可滲透之障壁;及 (b) 使用適當之複合材料包覆該自持性襯墊,以形成 一承載器皿,其與該自持性襯墊接觸,該承載器皿適於承 受約 1 03 5 kPa (150 psia)至約 7 5 90 kPa (1100 psia)之壓力 及約-123°C(-190°F)至約-62°C(-80°F)之溫度,且該複合材 料具有一熱膨脹係數,其(i)實質上與位於該自持性襯墊界 面之自持性襯墊的熱膨脹係數相同,且(i i)其跨經該承載 器皿之厚度隨著與該界面之距離的增加而逐漸降低。 8、 如申請專利範圍第7項之方法,其中該複合材料 係包含位於該自持性襯墊界面上之中間材料,其中該中間 材料具有適當之抗切強度或應變,以實質防止該容器於溫 度在環境溫度及約-123 t (-190°F )之間變化時損壞。 9、 如申請專利範圍第7項之方法,其中步驟(a)之自 持性襯墊係由基本上由鋁組成之材料製得,且該複合材料 係包含選自下列者之纖維(i)碳,(ii)玻璃,(iii)凱夫拉爾 (keWar),(iv)芳族聚醯胺,及(v)超高分子量聚乙烯。 10、 如申請專利範圍第7項之方法,其中步驟(a)之 自持性襯墊係由基本上由鋼組成之材料製得,其屈服強度 至少約690 MPa (100 ksi),其基材及焊接後之受熱區中的 延性-脆性轉變溫度低於約-62 °C (-8 0 °F),且該複合材料係 包含選自下列者之纖維(i)碳,(ii)玻璃,(iii)凱夫拉爾 (kevlar),(iv)芳族聚醯胺,及(v)超高分子量聚乙烯。 1281011 (4) f 1 1、一種製造容器之方法,該容器適用於約1 0 3 5 kPa (150 psia)至約 7590 kPa (1100 psia)之壓力及約-123°C ( _190Τ )至約- 62°C (-80°F )之溫度下儲存加壓液化天然氣, 該方法包括下列步驟: (a) 建構一自持性襯墊,該自持性襯墊適於針對該加 壓流體提供實質不可滲透之障壁;及 (b) 使用適當之複合材料包覆該自持性襯墊,以形成 一承載器皿,其與該自持性襯墊接觸,該承載器皿適於承 受約 1 03 5 kPa (150 psia)至約 75 90 kPa (1100 psia)之壓力 及約-123°C(-190°F)至約-62°C(-80°F)之溫度,且該複合材 料具有實質上與位於該自持性襯墊界面之自持性襯墊的熱 膨脹係數相同之熱膨脹係數。 12、一 種於約 1 03 5 kPa (150 psia)至約 75 90 kPa (1 100 psia)之壓力及約-123°C (-190°F )至約- 62t: (-80°F )之 溫度下儲存加壓液化天然氣之方法,該方法包括下列步驟 :將該加壓液化天然氣容裝於至少一容器中,該至少一容 器係包含(a) —自持性襯墊,該自持性襯墊係針對該加壓 流體提供實質不可滲透之障壁;及(b)—承載器皿,與該 自持性襯墊接觸,該承載器皿係自複合材料製得,且適於 承受約 1035 kPa (150 psia)至約 7590 kPa (11〇〇 pSia)之壓 力及約-123°C(-190°F)至約-62t:(-80°F)之溫度,且該複合 材料具有實質上與位於該自持性襯墊界面之自持性襯墊的 熱膨脹係數相同之熱膨脹係數。 1 3、如申請專利範圍第1 2項之方法,其中該複合材 -4- 1281011 … (5) β曰擊正+本 料之熱膨脹係數跨經該承載器皿之厚度隨著與該界面之距 離的增加而逐漸降低。 14、如申請專利範圍第12項之方法,其中該複合材 料係包含位於該自持性襯墊界面上之中間材料,其中該中 間材料具有適當之抗切強度或應變,以實質防止該容器於 溫度在環境溫度及約-123 °C (-190 °F )之間變化時損壞。 1 5、如申請專利範圍第1 2項之方法,其中該至少一 容器係包含(a) —自持性襯墊,由基本上由鋁組成之材料 製得,且針對該加壓流體提供實質不可滲透之障壁;且該 複合材料係包含選自下列者之纖維⑴碳,(Π)玻璃,(iii) 凱夫拉爾(kevlar),(iv)芳族聚醯胺,及(v)超高分子量聚 乙烯。 1 6、如申請專利範圍第 1 2項之方法,其中該至少一 容器係包含(a) —自持性襯墊,由基本上由鋼組成之材料 製得,其屈服強度至少約690 MPa (100 ksi),且基材及焊 接後之受熱區中的延性-脆性轉變溫度低於約-62 °C (-80 °F ) ’而針對該加壓流體提供實質不可滲透之障壁;且該複合 材料係包含選自下列者之纖維(i)碳,(ii)玻璃,(iii)凱夫 拉爾(kevlar),(iv)芳族聚醯胺,及(v)超高分子量聚乙烯1281011 (2) The mat is made of a material consisting essentially of aluminum, and the composite comprises fibers selected from the group consisting of (1) carbon, (ii) glass, (iii) kevlar, (iv) Aromatic polyamines, and (v) ultra high molecular weight polyethylene. 5. The container of claim 1, wherein the self-sustaining liner is made of a material consisting essentially of steel having a yield strength of at least about 690 MPa (100 ksi), the substrate and the heat after welding. The ductile-brittle transition temperature in the zone is less than about -62 °C (-80 °F), and the composite material comprises fibers selected from the group consisting of (1) carbon, (ii) glass, (iii) kevlar (kevlar) ), (iv) aromatic polyamines, and ultra high molecular weight polyethylene. 6. A container suitable for storing pressurized liquefied natural gas, using a pressure of from about 10 3 5 kPa (150 psia) to about 7 5 9 kPa (1100 psia) and about -123 ° C (-190 ° F) ) to a temperature of about -62 ° C (-80 ° F), the container comprising (a) a self-sustaining liner that provides a substantially impermeable barrier to the pressurized fluid; and (b) - a carrier vessel in contact with the self-sustaining liner, the carrier vessel being made from a composite material and adapted to withstand a pressure of from about 1 03 5 kPa (150 psia) to about 7590 kPa (1100 psia) and about 123 °〇: (-190°Ρ) to a temperature of about -62°C (-80°F), and the composite has substantially the same thermal expansion coefficient as the self-sustaining gasket at the interface of the self-sustaining gasket. . 7. A method of making a container suitable for a pressure of from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1 100 psia) and from about -123 t: (-190 °F) to about -62° Storage of pressurized fluid at a temperature of C (-80 °F), method 1281011 ...................................I _ 1丨厂:'· ”, (3) i1 ........——,” includes the following steps: (a) Construction of a self-contained gasket suitable for providing the pressurized fluid a substantially impermeable barrier; and (b) coating the self-sustaining liner with a suitable composite material to form a carrier that is in contact with the self-sustaining liner, the carrier being adapted to withstand about 1 03 5 kPa ( 150 psia) to a pressure of about 7 5 90 kPa (1100 psia) and a temperature of about -123 ° C (-190 ° F) to about -62 ° C (-80 ° F), and the composite has a coefficient of thermal expansion (i) is substantially the same as the coefficient of thermal expansion of the self-sustaining pad at the self-sustaining pad interface, and (ii) its thickness across the carrier vessel gradually decreases as the distance from the interface increases. 8. The method of claim 7, wherein the composite material comprises an intermediate material at the interface of the self-sustaining liner, wherein the intermediate material has suitable shear strength or strain to substantially prevent the container from being exposed to temperature. Damaged when the ambient temperature changes between approximately -123 t (-190 °F). 9. The method of claim 7, wherein the self-sustaining liner of step (a) is made of a material consisting essentially of aluminum, and the composite material comprises fibers selected from the group consisting of: (i) carbon (ii) glass, (iii) keWar, (iv) aromatic polyamine, and (v) ultra high molecular weight polyethylene. 10. The method of claim 7, wherein the self-sustaining liner of step (a) is made of a material consisting essentially of steel having a yield strength of at least about 690 MPa (100 ksi), the substrate and The ductile-brittle transition temperature in the heated zone after welding is less than about -62 °C (-8 0 °F), and the composite material comprises fibers (i) carbon selected from the group consisting of (ii) glass, ( Iii) kevlar, (iv) aromatic polyamines, and (v) ultrahigh molecular weight polyethylene. 1281011 (4) f 1 1. A method of making a container suitable for a pressure of from about 10 3 5 kPa (150 psia) to about 7590 kPa (1100 psia) and about -123 ° C ( _190 Τ ) to about - Storage of pressurized liquefied natural gas at a temperature of 62 ° C (-80 ° F), the method comprising the steps of: (a) constructing a self-contained liner adapted to provide substantial impermeability to the pressurized fluid And (b) coating the self-sustaining liner with a suitable composite material to form a carrier vessel that is in contact with the self-sustaining liner, the carrier vessel being adapted to withstand about 1 03 5 kPa (150 psia) a pressure of about 75 90 kPa (1100 psia) and a temperature of about -123 ° C (-190 ° F) to about -62 ° C (-80 ° F), and the composite material is substantially in self-sustaining The self-sustaining pad of the pad interface has the same coefficient of thermal expansion as the coefficient of thermal expansion. 12. A pressure of from about 1 03 5 kPa (150 psia) to about 75 90 kPa (1 100 psia) and a temperature of from about -123 ° C (-190 ° F) to about - 62 t: (-80 ° F) A method of storing pressurized liquefied natural gas, the method comprising the steps of: accommodating the pressurized liquefied natural gas in at least one container, the at least one container comprising (a) a self-sustaining gasket, the self-sustaining gasket Providing a substantially impermeable barrier to the pressurized fluid; and (b) a carrier vessel in contact with the self-sustaining liner, the carrier being fabricated from a composite material and adapted to withstand about 1035 kPa (150 psia) to a pressure of about 7590 kPa (11 〇〇 pSia) and a temperature of about -123 ° C (-190 ° F) to about -62 t: (-80 ° F), and the composite material has substantially the same self-sustaining lining The self-sustaining pad of the pad interface has the same coefficient of thermal expansion as the coefficient of thermal expansion. 1 3. The method of claim 12, wherein the composite material -4-1281011 (5) β slamming positive + the thermal expansion coefficient of the material spans the thickness of the carrier vessel and the distance from the interface The increase is gradually decreasing. 14. The method of claim 12, wherein the composite material comprises an intermediate material at the interface of the self-sustaining liner, wherein the intermediate material has suitable shear strength or strain to substantially prevent the container from being exposed to temperature. Damaged when the ambient temperature changes between approximately -123 °C (-190 °F). The method of claim 12, wherein the at least one container comprises (a) a self-sustaining liner made of a material consisting essentially of aluminum and providing substantially no a barrier to penetration; and the composite material comprises fibers (1) carbon, (Π) glass, (iii) kevlar, (iv) aromatic polyamine, and (v) ultrahigh molecular weight selected from the group consisting of Polyethylene. The method of claim 12, wherein the at least one container comprises (a) a self-sustaining liner made of a material consisting essentially of steel having a yield strength of at least about 690 MPa (100). Ksi), and the ductile-brittle transition temperature in the substrate and the heated zone after soldering is less than about -62 °C (-80 °F) and provides a substantially impermeable barrier to the pressurized fluid; and the composite Is a fiber comprising (i) carbon selected from the group consisting of (ii) glass, (iii) kevlar, (iv) aromatic polyamine, and (v) ultrahigh molecular weight polyethylene
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