JP2019098325A - 流体分配装置 - Google Patents
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- JP2019098325A JP2019098325A JP2018218197A JP2018218197A JP2019098325A JP 2019098325 A JP2019098325 A JP 2019098325A JP 2018218197 A JP2018218197 A JP 2018218197A JP 2018218197 A JP2018218197 A JP 2018218197A JP 2019098325 A JP2019098325 A JP 2019098325A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
- F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/0605—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the feed stream
- F25J3/061—Natural gas or substitute natural gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0209—Natural gas or substitute natural gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0233—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0238—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 2 carbon atoms or more
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0242—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 3 carbon atoms or more
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/0695—Start-up or control of the process; Details of the apparatus used
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2280/00—Control of the process or apparatus
- F25J2280/02—Control in general, load changes, different modes ("runs"), measurements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/32—Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
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- Oil, Petroleum & Natural Gas (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Loading And Unloading Of Fuel Tanks Or Ships (AREA)
- Devices For Dispensing Beverages (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
本出願は、その内容が参照により本明細書に援用される、2017年11月29日出願の米国仮出願第62/591,948号の利益を主張する。
Claims (20)
- 処理構成要素に流体を分配する装置であって、
a.流体の流れを受けるように構成される入口ポートを有する容器と、
b.前記容器の上部空間と流体連通するように、前記容器と流体連通している蒸気出口管入口を前記入口ポートより上に有する蒸気出口管であって、前記流体処理構成要素と流体連通して配置されるようにも構成される、蒸気出口管と、
c.前記容器の液体側と流体連通する液体出口管入口を有する液体出口管であって、前記流体処理構成要素と流体連通して配置されるようにも構成される、液体出口管と、
d.前記容器の前記液体側と流体連通しているバイパス管入口、および前記蒸気出口管と流体連通しているバイパス管出口を有するバイパス管であって、
i)前記容器内の液面が所定のレベルに到達したとき、液体が前記バイパス管を通って前記蒸気出口管へと進み、その結果、液面が前記入口ポートから前記容器に入る際、上部空間が前記液面より上に保たれるように構成され、
ii)前記容器内の液面が前記所定のレベルより下であるとき、液体が前記バイパス管から前記蒸気出口管へと進まないように構成される、
バイパス管と、
を備える、装置。 - 前記容器が、上方部および下方部を有し、前記蒸気出口管が、前記入口ポートより上で前記容器の前記上方部に連結され、前記液体出口管が、前記容器の前記下方部に連結される、請求項1に記載の装置。
- 前記容器の液体側と流体連通するように、前記容器の前記下方部に連結される2つ以上の液体出口管をさらに備え、前記2つ以上の液体出口管が、前記流体処理構成要素と流体連通して配置されるようにも構成される、請求項2に記載の装置。
- 前記バイパス管が、前記バイパス管と、前記バイパス管と前記蒸気出口管の間の接合部の垂直下方にある前記容器の前記下方部との間の接合部を介して、前記容器の前記下方部と流体連通している、請求項2に記載の装置。
- 前記バイパス管が、前記バイパス管と、前記バイパス管と前記蒸気出口管の間の接合部の垂直下方にある前記容器液体出口管との間の接合部を介して、前記容器の前記下方部と流体的に通じた状態である、請求項2に記載の装置。
- 前記バイパス管出口が、接合部において前記蒸気出口管と流体連通していて、前記接合部が、前記容器蒸気出口ポートの垂直下方に位置決めされる、請求項1に記載の装置。
- 前記バイパス管が、前記容器の中に位置決めされた細長いパイプ部を含み、前記細長いパイプ部が、前記バイパス管入口を含む下端部と、前記蒸気出口管と流体連通していて上端部とを有する、請求項1に記載の装置。
- 前記容器が、側壁を含み、前記バイパス管が、前記容器側壁を通って、前記蒸気出口管と前記細長いパイプ部との間に延在する分岐部をさらに含む、請求項7に記載の装置。
- 前記容器が、側壁を含み、前記蒸気出口管が、前記容器内に位置決めされかつ前記蒸気出口管入口を含む上方パイプ部を含み、前記蒸気出口管が、前記容器側壁を通って延在しかつ前記上方パイプ部と流体連通していて分岐部をさらに含む、請求項1に記載の装置。
- 前記バイパス管が、前記容器内に位置決めされかつ前記バイパス管入口および前記バイパス管出口を含む下方パイプ部を含む、請求項9に記載の装置。
- 前記上方パイプ部および前記下方パイプ部が、前記容器内に位置決めされた単一のパイプ部材によって形成される、請求項10に記載の装置。
- a.熱交換器と、
b.前記熱交換器に前記流体を分配する装置であって、
i.流体の流れを受けるように構成される入口ポートを有する容器と、
ii.前記容器の上部空間と流体連通するように、前記容器流体連通している蒸気出口管入口を前記入口ポートより上に有する蒸気出口管であって、前記熱交換器へと流体を向かわせるようにも構成される、蒸気出口管と、
iii.前記容器の液体側と流体連通する液体出口管入口を有する液体出口管であって、前記熱交換器へと流体を向かわせるようにも構成される、液体出口管と、
iv.前記容器の前記液体側と流体連通しているバイパス管入口、および前記蒸気出口管と流体連通しているバイパス管出口と、を有するバイパス管であって、
1.前記容器内の液面が所定のレベルに到達したとき、液体が前記バイパス管を通って前記蒸気出口管へと進み、その結果、液体が前記入口ポートから前記容器に入る際、上部空間が前記液面より上に保たれるように構成され、
2.前記容器内の液面が前記所定のレベルより下であるとき、液体が前記バイパス管から前記蒸気出口管へと進まないように構成される、
バイパス管と、
を含む装置と、
を備える、流体処理システム。 - 前記容器の液体側と流体連通するように、前記容器の前記下方部に連結される2つ以上の液体出口管をさらに備え、前記2つ以上の液体出口管が、前記流体処理構成要素流体連通して配置されるようにも構成される、請求項12に記載の装置。
- 前記容器が、上方部および下方部を有し、前記蒸気出口管が、前記入口ポートより上で前記容器の前記上方部に連結され、前記液体出口管が、前記容器の前記下方部に連結される、請求項12に記載の装置。
- 前記バイパス管が、前記バイパス管と、前記バイパス管と前記蒸気出口管の間の接合部の垂直下方にある前記容器の前記下方部との間の接合部を介して、前記容器の前記下方部と流体連通している、請求項14に記載の装置。
- 前記バイパス管が、前記バイパス管と、前記バイパス管と前記蒸気出口管の間の接合部の垂直下方にある前記容器液体出口管との間の接合部を介して、前記容器の前記下方部と流体連通している、請求項14に記載の装置。
- 前記バイパス管出口が、接合部において前記蒸気出口管と流体連通していて、前記接合部が、前記容器蒸気出口ポートの垂直下方に位置決めされる、請求項12に記載の装置。
- 前記容器が、側壁を含み、前記バイパス管が、前記容器の中に位置決めされた細長いパイプ部を含み、前記細長いパイプ部が、前記バイパス管入口を含む下端部分、および前記容器側壁を通って前記蒸気出口管と前記細長いパイプ部の上部部分との間に延在する分岐部を有する、請求項12に記載の装置。
- 前記容器が、側壁を含み、前記蒸気出口管が、前記容器内に位置決めされかつ前記蒸気出口管入口を含む上方パイプ部を含み、前記蒸気出口管が、前記容器側壁を通って延在しかつ前記上方パイプ部および前記熱交換器と流体連通している分岐部をさらに含み、前記バイパス管が、前記容器内に位置決めされかつ前記バイパス管入口および前記バイパス管出口を含む下方パイプ部を含み、前記上方パイプ部および下方パイプ部が、前記容器内に位置決めされた単一のパイプ部材によって形成される、請求項12に記載の装置。
- 処理構成要素に流体を分配する方法であって、
a.分配装置へと流体流れを受けるステップと、
b.前記流体流れが混相の流れである場合、前記受けた流体流れを蒸気流れおよび液体流れに分離し、液体経路に沿って前記処理構成要素へと前記液体流れを向かわせ、蒸気経路に沿って前記処理構成要素へと前記蒸気流れを向かわせるステップと、
c.前記受けた流体流れが、全体としてすべて液体の流れである場合、前記液体経路と前記蒸気経路の両方に沿って前記処理構成要素へと液体流れを送り出すステップと、
を含む、方法。
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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US201762591948P | 2017-11-29 | 2017-11-29 | |
US62/591,948 | 2017-11-29 | ||
US16/145,654 US10883761B2 (en) | 2017-11-29 | 2018-09-28 | Fluid distribution device |
US16/145,654 | 2018-09-28 |
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JP2019098325A true JP2019098325A (ja) | 2019-06-24 |
JP7258521B2 JP7258521B2 (ja) | 2023-04-17 |
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US (1) | US10883761B2 (ja) |
JP (1) | JP7258521B2 (ja) |
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Citations (5)
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US2479070A (en) * | 1943-06-19 | 1949-08-16 | Linde Air Prod Co | Apparatus for and method of dispensing liquefied gases |
US5163409A (en) * | 1992-02-18 | 1992-11-17 | Minnesota Valley Engineering, Inc. | Vehicle mounted LNG delivery system |
US5771946A (en) * | 1992-12-07 | 1998-06-30 | Chicago Bridge & Iron Technical Services Company | Method and apparatus for fueling vehicles with liquefied cryogenic fuel |
US6640554B2 (en) * | 2001-04-26 | 2003-11-04 | Chart Inc. | Containment module for transportable liquid natural gas dispensing station |
JP2014109384A (ja) * | 2012-11-30 | 2014-06-12 | Chart Inc | 極低温液体分配システムのための熱管理システムおよび方法 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3919859A (en) * | 1974-11-18 | 1975-11-18 | Phillips & Co H A | Refrigerating system |
JPS5984050A (ja) * | 1982-11-06 | 1984-05-15 | 株式会社日立製作所 | 冷凍装置 |
JPS60262A (ja) * | 1983-06-17 | 1985-01-05 | 株式会社日立製作所 | 冷凍サイクル |
US6973797B2 (en) * | 2004-05-10 | 2005-12-13 | York International Corporation | Capacity control for economizer refrigeration systems |
-
2018
- 2018-09-28 US US16/145,654 patent/US10883761B2/en active Active
- 2018-11-14 DE DE102018219416.5A patent/DE102018219416A1/de active Pending
- 2018-11-14 FR FR1860491A patent/FR3074066B1/fr active Active
- 2018-11-21 JP JP2018218197A patent/JP7258521B2/ja active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2479070A (en) * | 1943-06-19 | 1949-08-16 | Linde Air Prod Co | Apparatus for and method of dispensing liquefied gases |
US5163409A (en) * | 1992-02-18 | 1992-11-17 | Minnesota Valley Engineering, Inc. | Vehicle mounted LNG delivery system |
US5771946A (en) * | 1992-12-07 | 1998-06-30 | Chicago Bridge & Iron Technical Services Company | Method and apparatus for fueling vehicles with liquefied cryogenic fuel |
US6640554B2 (en) * | 2001-04-26 | 2003-11-04 | Chart Inc. | Containment module for transportable liquid natural gas dispensing station |
JP2014109384A (ja) * | 2012-11-30 | 2014-06-12 | Chart Inc | 極低温液体分配システムのための熱管理システムおよび方法 |
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FR3074066B1 (fr) | 2023-04-14 |
DE102018219416A1 (de) | 2019-05-29 |
US10883761B2 (en) | 2021-01-05 |
US20190162470A1 (en) | 2019-05-30 |
JP7258521B2 (ja) | 2023-04-17 |
FR3074066A1 (fr) | 2019-05-31 |
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