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公开(公告)号：WO2006112977A3
公开(公告)日：2009-06-04
申请号：PCT/US2006008873
申请日：2006-03-14
Applicant: KNAEBEL KENT S
Inventor： KNAEBEL KENT S
IPC: B01D53/08
CPC classification number: B01D53/0462 , B01D53/08 , B01D53/261 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/116 , B01D2253/304 , B01D2256/10 , B01D2256/24 , B01D2256/245 , B01D2257/302 , B01D2257/404 , B01D2257/504 , B01D2257/602 , B01D2257/702 , B01D2257/80 , B01D2259/40007 , B01D2259/40098 , Y02C10/08 , Y02E50/346
Abstract: A method for removing one or more strongly adsorbed components (SAC) from a process gas stream having SAC and other gaseous components adjusts the temperature of the SAC-laden process gas stream to be between about 80°C and about 500°C. The temperature-adjusted process gas stream is contacted with a heat-exchange surface to transfer heat to an adsorbent, thus causing adsorbed SAC to be desorbed for collection, and to cool the process gas stream and remove any condensate from the cooled process gas stream. The cooled process gas stream is contacted with a cooled section of the adsorbent to adsorb SAC therefrom, producing a SAC-depleted process gas stream and a SAC-laden adsorbent. Desorbed SAC is withdrawn for collection and any adsorbent fines are withdrawing for collection.
Abstract translation: 从具有SAC和其它气体组分的工艺气流中除去一种或多种强吸附组分（SAC）的方法将含SAC的工艺气流的温度调节在约80℃至约500℃之间。 温度调节的工艺气体流与热交换表面接触以将热量传递到吸附剂，从而引起吸附的SAC被解吸以进行收集，并且冷却工艺气体流并从冷却的工艺气体流中除去任何冷凝物。 冷却的工艺气流与吸附剂的冷却部分接触以从其吸附SAC，产生SAC贫化的工艺气体流和含SAC的吸附剂。 解吸SAC撤回收集，任何吸附剂细粉都被取出收集。
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Patent Agency Ranking
公开(公告)号：WO2007038581A1
公开(公告)日：2007-04-05
申请号：PCT/US2006/037650
申请日：2006-09-27
Applicant: BASF AKTIENGESELLSCHAFT , VIRANI, Naheed , SEAGRAVES, Thomas , MUSSELMAN, Wayne, David , CHAN, William, Stewart , KNAEBEL, Kent, S. , SHIN, Heungsoo
Inventor： VIRANI, Naheed , SEAGRAVES, Thomas , MUSSELMAN, Wayne, David , CHAN, William, Stewart , KNAEBEL, Kent, S. , SHIN, Heungsoo
CPC classification number: C01B21/1418 , B01D53/047 , B01D2257/402 , Y02C20/10 , Y02P20/153
Abstract: Hydroxylamine is formed in a reactor through a partial hydrogenation of nitric oxide gas (NO) with hydrogen gas (H 2 ) in an aqueous medium with nitrogen gas (N 2 ) as an inert gas. The formation of the hydroxylamine forms nitrous oxide gas (N 2 O). The gases and the water vapor are flowed away from the reactor in a vent gas stream enabling recycling of the gases. The N 2 O is removed from the vent gas stream to reduce flammability. Once the N 2 O is removed, the NO, H 2 , and N 2 are recycled and re-used in the reactor to form additional hydroxylamine. The N 2 O removed from the vent gas stream can be commercially sold or economically discarded.
Abstract translation: 羟胺在反应器中通过在氮气（N 2/2）的水性介质中将一氧化氮气体（NO）与氢气（H 2 H 2）部分氢化形成为反应器， 惰性气体。 羟胺的形成形成一氧化二氮气体（N 2 O 2）。 气体和水蒸气以能够再循环气体的排气气流从反应器中流出。 从排出气流中除去N 2 O 2以降低可燃性。 一旦去除了N 2 O 2，则NO，H 2 N 2和N 2 O 2被再循环并重新用于反应器以形成额外的 羟胺。 从排放气流中除去的N 2 O 2可以商业销售或经济地丢弃。
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公开(公告)号：WO2007038661B1
公开(公告)日：2007-08-02
申请号：PCT/US2006037797
申请日：2006-09-27
Applicant: BASF AG , VIRANI NAHEED , SEAGRAVES THOMAS , MUSSELMAN WAYNE DAVID , CHAN WILLIAM STEWART , KNAEBEL KENT S , SHIN HEUNGSOO
Inventor： VIRANI NAHEED , SEAGRAVES THOMAS , MUSSELMAN WAYNE DAVID , CHAN WILLIAM STEWART , KNAEBEL KENT S , SHIN HEUNGSOO
IPC: B01D53/047
CPC classification number: B01D53/047 , B01D53/053 , B01D53/261 , B01D2257/402 , B01D2257/404 , B01D2257/80 , B01D2259/40001 , B01D2259/40052 , B01D2259/40081 , B01D2259/402 , B01D2259/404 , Y02C20/10
Abstract: Hydroxylamine is formed in a reactor through a partial hydrogenation of nitric oxide gas (NO) with hydrogen gas (H 2 ) in an aqueous medium with nitrogen gas (N 2 ) as an inert gas. The formation of the hydroxylamine forms nitrous oxide gas (N 2 O). The gases and the water vapor are flowed away from the reactor in a vent gas stream enabling recycling of the gases. The N 2 O is removed from the vent gas stream to reduce flammability. The method of removing N 2 O comprises the steps of (a) flowing the vent gas through a nitrous oxide adsorbent material comprising particles such that the N 2 O is adsorbed onto the particles; (b) forming a buffer zone comprising N 2 adjacent to the nitrous oxide adsorbent material; (c) flowing additional N2O through the nitrous oxide adsorbent material to displace the other gas; and (d) desorbing the N 2 O from the nitrous oxide adsorbent material. Once the N 2 O is removed, the NO, H 2 , and N 2 are recycled and re-used in the reactor to form additional hydroxylamine. The N 2 O removed from the vent gas stream is of high purity and can be commercially sold or economically discarded.
Abstract translation: 羟胺在反应器中通过在氮气（N 2/2）的水性介质中将一氧化氮气体（NO）与氢气（H 2 H 2）部分氢化形成为反应器， 惰性气体。 羟胺的形成形成一氧化二氮气体（N 2 O 2）。 气体和水蒸气以能够再循环气体的排气气流从反应器中流出。 从排出气流中除去N 2 O 2以降低可燃性。 除去N 2 O O的方法包括以下步骤：（a）使排出气体流过包含颗粒的一氧化二氮吸附剂材料，使得N 2 O 2吸附在 粒子; （b）形成与一氧化二氮吸附剂材料相邻的包含N 2 N的缓冲区; （c）通过一氧化二氮吸附材料流动额外的N2O以置换其他气体; 和（d）从一氧化二氮吸附剂材料中解吸N 2 O 3。 一旦去除了N 2 O 2，则NO，H 2 N 2和N 2 O 2被再循环并重新用于反应器以形成额外的 羟胺。 从排出气流中除去的N 2 O 2是高纯度的，可以商业销售或经济地丢弃。
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公开(公告)号：WO2007038661A1
公开(公告)日：2007-04-05
申请号：PCT/US2006/037797
申请日：2006-09-27
Applicant: BASF AKTIENGESELLSCHAFT , VIRANI, Naheed , SEAGRAVES, Thomas , MUSSELMAN, Wayne, David , CHAN, William, Stewart , KNAEBEL, Kent, S. , SHIN, Heungsoo
Inventor： VIRANI, Naheed , SEAGRAVES, Thomas , MUSSELMAN, Wayne, David , CHAN, William, Stewart , KNAEBEL, Kent, S. , SHIN, Heungsoo
IPC: B01D53/047
CPC classification number: B01D53/047 , B01D53/053 , B01D53/261 , B01D2257/402 , B01D2257/404 , B01D2257/80 , B01D2259/40001 , B01D2259/40052 , B01D2259/40081 , B01D2259/402 , B01D2259/404 , Y02C20/10
Abstract: Hydroxylamine is formed in a reactor through a partial hydrogenation of nitric oxide gas (NO) with hydrogen gas (H 2 ) in an aqueous medium with nitrogen gas (N 2 ) as an inert gas. The formation of the hydroxylamine forms nitrous oxide gas (N 2 O). The gases and the water vapor are flowed away from the reactor in a vent gas stream enabling recycling of the gases. The N 2 O is removed from the vent gas stream to reduce flammability. The method of removing N 2 O comprises the steps of (a) flowing the vent gas through a nitrous oxide adsorbent material comprising particles such that the N 2 O is adsorbed onto the particles; (b) forming a buffer zone comprising N 2 adjacent to the nitrous oxide adsorbent material; (c) flowing additional N2O through the nitrous oxide adsorbent material to displace the other gas; and (d) desorbing the N 2 O from the nitrous oxide adsorbent material. Once the N 2 O is removed, the NO, H 2 , and N 2 are recycled and re-used in the reactor to form additional hydroxylamine. The N 2 O removed from the vent gas stream is of high purity and can be commercially sold or economically discarded.
Abstract translation: 羟胺在反应器中通过用氮气（N
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公开(公告)号：WO2006112977A2
公开(公告)日：2006-10-26
申请号：PCT/US2006/008873
申请日：2006-03-14
Applicant: KNAEBEL, Kent, S.
Inventor： KNAEBEL, Kent, S.
IPC: B01D53/02
CPC classification number: B01D53/0462 , B01D53/08 , B01D53/261 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/116 , B01D2253/304 , B01D2256/10 , B01D2256/24 , B01D2256/245 , B01D2257/302 , B01D2257/404 , B01D2257/504 , B01D2257/602 , B01D2257/702 , B01D2257/80 , B01D2259/40007 , B01D2259/40098 , Y02C10/08 , Y02E50/346
Abstract: A method for removing one or more strongly adsorbed components (SAC) from a process gas stream having SAC and other gaseous components adjusts the temperature of the SAC-laden process gas stream to be between about 80°C and about 500°C. The temperature-adjusted process gas stream is contacted with a heat-exchange surface to transfer heat to an adsorbent, thus causing adsorbed SAC to be desorbed for collection, and to cool the process gas stream and remove any condensate from the cooled process gas stream. The cooled process gas stream is contacted with a cooled section of the adsorbent to adsorb SAC therefrom, producing a SAC-depleted process gas stream and a SAC-laden adsorbent. Desorbed SAC is withdrawn for collection and any adsorbent fines are withdrawing for collection.
Abstract translation: 从具有SAC和其它气体组分的工艺气流中除去一种或多种强吸附组分（SAC）的方法将含SAC的工艺气流的温度调节在约80℃至约500℃之间。 温度调节的工艺气体流与热交换表面接触以将热量传递到吸附剂，从而引起吸附的SAC被解吸以进行收集，并且冷却工艺气体流并从冷却的工艺气体流中除去任何冷凝物。 冷却的工艺气流与吸附剂的冷却部分接触以从其吸附SAC，产生SAC贫化的工艺气体流和含SAC的吸附剂。 解吸SAC撤回收集，任何吸附剂细粉都被取出收集。
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公开(公告)号：WO2011059451A1
公开(公告)日：2011-05-19
申请号：PCT/US2009/064518
申请日：2009-11-16
Applicant: KENT KNAEBEL & ASSOCIATES, INC. , KNAEBEL, Kent, S.
Inventor： KNAEBEL, Kent, S.
IPC: B01D53/047
CPC classification number: B01D53/0462 , B01D53/047 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2256/245 , B01D2257/102 , B01D2257/104 , B01D2257/504 , B01D2257/80 , B01D2258/05 , B01D2259/40066 , B01D2259/403 , B01D2259/404 , Y02C10/08 , Y02E50/343 , Y02E50/346
Abstract: Methane product gas is produced from landfill gas and gob gas either by a three-stage process of PSA-TSA-PSA or PSA-PSA-PSA, or a two-stage process of PSA-PSA.
Abstract translation: 甲烷产物气体通过PSA-TSA-PSA或PSA-PSA-PSA的三阶段方法或PSA-PSA的两阶段方法由填埋气体和气体气体产生。
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