公开(公告)号：US20180200666A1

公开(公告)日：2018-07-19

申请号：US15410024

申请日：2017-01-19

申请人： Larry Baxter ,  Aaron Sayre ,  Stephanie Burt ,  Nathan Davis

发明人： Larry Baxter ,  Aaron Sayre ,  Stephanie Burt ,  Nathan Davis

IPC分类号： B01D53/14 ,  B01D53/62 ,  B01D53/96 ,  C10L3/10 ,  F25J3/06

CPC分类号： B01D53/1475 ,  B01D53/002 ,  B01D53/1493 ,  B01D53/62 ,  B01D2251/302 ,  B01D2251/306 ,  B01D2251/402 ,  B01D2251/404 ,  B01D2251/80 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/202 ,  B01D2252/2021 ,  B01D2252/2023 ,  B01D2252/504 ,  B01D2257/504 ,  B01D2258/0283 ,  C10L3/104 ,  C10L2290/12 ,  C10L2290/541 ,  Y02C10/04 ,  Y02C10/06 ,  Y02C10/12

摘要： A method for continuously removing carbon dioxide vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the carbon dioxide vapor. A combination of chemical effects cause the carbon dioxide to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the carbon dioxide vapor's condensation point, whereby the carbon dioxide condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the carbon dioxide vapor and thereby extracts at least a portion of the carbon dioxide vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the carbon dioxide's condensation point, and wherein at least one component forms a chemical complex with the carbon dioxide vapor and thereby extracts at least a portion of the carbon dioxide vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the carbon dioxide vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the carbon dioxide vapor removed.

公开(公告)号：US20190168175A1

公开(公告)日：2019-06-06

申请号：US15833279

申请日：2017-12-06

申请人： Larry Baxter ,  Aaron Sayre ,  Seth Babcock ,  Nathan Davis

发明人： Larry Baxter ,  Aaron Sayre ,  Seth Babcock ,  Nathan Davis

IPC分类号： B01F5/04 ,  B01D7/00 ,  B01D53/00 ,  B01F3/04 ,  B01D25/12 ,  F25J3/08

摘要： Devices, systems, and methods for siphoning heat exchange or reaction for solids production are disclosed. Passing a contact fluid through a siphoning device, wherein the siphoning device is made of a contact fluid inlet, a carrier fluid inlet, and an outlet, and wherein the contact fluid passes through the contact fluid inlet, inducing a siphon in the carrier fluid inlet. This siphon then siphons a carrier fluid through the carrier fluid inlet and into the contact fluid. The carrier fluid is, in part, made of a first component. The carrier fluid and the contact fluid mix. This mixing produces a product solid, wherein the product solid is produced from the first component by desublimation, condensation, solidification, crystallization, precipitation, reaction with the contact fluid, or a combination thereof of at least a portion of the first component. The product solid passes through the outlet.

公开(公告)号：US20190060819A1

公开(公告)日：2019-02-28

申请号：US15683074

申请日：2017-08-22

申请人： Larry Baxter ,  Aaron Sayre

发明人： Larry Baxter ,  Aaron Sayre

IPC分类号： B01D47/02 ,  F28C3/06 ,  F28F13/12

摘要： A device and a method for contacting gases and liquids in the presence of entrained solids is disclosed. A vertical, cylindrical vessel of a first diameter with a bubbling apparatus is provided comprising an outer apparatus diameter, surrounded by an annular space, a height above the bottom of the vessel. The outer apparatus diameter is between ⅓ and ¾ of the first diameter. The height is less than ½ of the difference between the first diameter and the outer apparatus diameter. The carrier gas bubbles upward out of the bubbling apparatus. A fluid passing through the vessel transitions from turbulent, to laminar or transitional, back to turbulent flow due to the changes in flow path areas.