Chemical analysis method using reaction container

• US 4,040,786 A
• Filed: 02/12/1976
• Issued: 08/09/1977
• Est. Priority Date: 05/16/1975
• Status: Expired due to Term

• Current Assignee: Technicon Instruments Corporation (Bayer AG)
• Original Assignee: Worthington Biochemical Corporation
• Inventors: Trivedi, Ramesh C., Bungay, Henry R. III, Cuccolo, Paul J.
• Primary Examiner(s): Serwin, R.E.
• Application Number:
  US05/657,635
• Time in Patent Office: 544 Days
• Field of Search: 23/230 R, 23/253 R, 23/259, 23/292, 195/103.5 R, 206/223, 356/246
• US Class Current: 436/34
• CPC Class Codes: G01N 21/03 Cuvette constructions
• CPC Class Codes: Y10S 435/808 Optical sensing apparatus

Abstract

For use in measuring the extent or rate of optical density change produced by a reaction a rigid or semi-rigid disposable reaction container is disclosed of the type comprising a windowed reaction chamber adapted for the transmission of light therethrough and an auxiliary chamber that is separated from the reaction chamber except for an opening which is small enough to prevent substantial diffusion or movement of liquid from one chamber to the other when under static conditions but through which a solution of a reagent in the auxiliary chamber may be forced so as to enter the reaction chamber and commingle with a solution of another reagent and thereby trigger a reaction, improvements comprising the provision in a receptacle having side walls, end walls and a bottom wall of a projection which extends a substantial distance upwardly from the bottom wall so as to separate the lower part of the receptacle into two portions adapted to separate liquid in one of said portions from the other portion in combination with a cover having a downwardly depending divider which terminates in closely adjacent spaced relation to said projection, said projection and said divider separating said receptacle into a reaction chamber and an auxiliary chamber separated from each other except for the opening or passage that is provided by said closely spaced relation between said projection and the lower end of said divider. The parts preferably are dimensioned and arranged so that said opening is in the form of a passage of substantial length and is positioned so that nearly all of a solution in the auxiliary chamber may be forced therethrough into the reaction chamber. The receptacle preferably is in the form of one molded piece and, as said, the cover is sealed in place with a lyophilized reagent in at least one of the chambers. Preferably the aforesaid passage is of such restricted cross-section as to prevent gravitational flow of aqueous liquid from one of said chambers to the other when the level of liquid in said chamber is substantially above the uppermost portion of said passage and is substantially above the level of any liquid in the other chamber while being large enough to permit, responsive to applied pressure, the forcing of aqueous liquid through said passage so as to be injected into the other chamber and thereby become commingled with liquid in the other chamber.

Claims

1. In a method for measuring the extent of reaction between reaction reagents respectively contained in aqueous solutions wherein said solutions are commingled and the extent of reaction initiated by said commingling is measured by measuring the amount of change in optical density that follows said commingling and said solutions are respectively contained in two chambers of a reaction container and are commingled by one of said solutions being forced through an open passage between the two chambers into solution in the other chamber the steps of simultaneously introducing solutions of different reagents respectively into said chambers through openings at the top of said chambers essentially without travel of either solution through said open passage into the other chamber and simultaneously reducing the reagents dissolved in said solutions to the solid state by lyophilization.

2. The method according to claim 1 wherein during introduction of said solutions respectively into said chambers the liquid levels of said solutions are maintained essentially the same in said chambers.

3. The method according to claim 1 wherein said open passage is in the form of an elongated passage and wherein during the introduction of said solutions respectively into said chambers a quantity of air is entrapped in said passage which separates said solutions from each other in said passage.

4. The method according to claim 1 which includes the redissolving of said reagents by the simultaneous introduction of aqueous liquid into said chambers essentially without travel of aqueous liquid containing dissolved reagent from one chamber to the other prior to said forcing of solution from one chamber to the other as aforesaid through said open passage.

5. In a method for measuring the extent of reactions between reaction reagents respectively contained in aqueous solutions wherein said solutions are commingled and the extent of reaction initiated by said commingling is measured by measuring the amount of change in optical density that follows said commingling and said solutions are respectively contained in two chambers of a reaction container and are commingled by one of said solutions being forced from one of said chambers into the other chamber through an open passage having at each end an entrance respectively opening into each of said chambers, the steps of disposing different reagents, each in the solid state, respectively in said chambers and thereafter dissolving said reagents by simultaneous introduction of an aqueous liquid into said chambers to a level in each chamber substantially above the entrance of said passage into said chamber without travel of aqueous solution containing dissolved reagent from one chamber to the other through said open passage.

6. In a method for measuring the extent of reactions between reaction reagents respectively contained in aqueous solutions wherein said solutions are commingled and the extent of reaction initiated by said commingling is measured by measuring the amount of change in optical density that follows said commingling and said solutions are respectively contained in two chambers of a reaction container and are commingled by one of said solutions being forced from one of said chambers into the other chamber through an open passage having at each end an entrance respectively opening into each of said chambers, the steps of disposing different reagents, each in the solid state, respectively in said chambers and dissolving said reagents by introduction of aqueous liquid into each of said chambers to a level in each chamber substantially above the entrance of said passage into each chamber with entrapment of a quantity of air in said open passage which quantity of air separates said solutions from each other in said passage thereby preventing any commingling of said solutions in said open passage until one of said solutions is forced from one chamber through said open passage into the other chamber.

7. The method according to claim 6 wherein a portion of said open passage is disposed above the level of the entrance of said open passage into each chamber and said quantity of entrapped air is entrapped in said portion of said open passage.

8. In a method for measuring the extent of reaction between reaction reagents respectively contained in aqueous solutions wherein said solutions are commingled and the extent of reactions initiated by said commingling is measured by measuring the amount of change in optical density that follows said commingling and said solutions are respectively contained in two chambers of a reaction container and are commingled by one of said solutions being forced from one of said chambers into the other chamber through an open passage having at each end an entrance respectively opening into each of said chambers, the steps of introducing solutions of different reagents respectively into each of said chambers through an opening at the top of each chamber to a level above that of the entrance of said open passage into said chamber with entrapment of a quantity of air in said open passage that separates said solutions from each other in said open passage, and thereafter reducing said solutions to dryness in each of said chambers by lyophilization.

9. The method according to claim 8 wherein a portion of said open passage is disposed above the level of the entrance of the passage into each chamber and said quantity of entrapped air is entrapped in said portion of the passage.

10. The method according to claim 9 wherein the lyophilized reagent in each of said chambers is reconstituted by the introduction of an aqueous liquid into each chamber through an opening at the top thereof to a level above the level of the entrance of said open passage into said chamber with entrapment of a quantity of air in said portion of said open passage which separates the reconstituted solutions from each other in said open passage until one of the reconstituted solutions is forced through said open passage to commingle it with reconstituted solution in the other chamber.

11. In a disposable reaction container which is composed essentially of rigid or semi-rigid material and which presents interior surfaces that define two upstanding laterally adjacent chambers having dividing means therebetween that separate said chambers from each other except for an open passage between said chambers the entrances of which respectively into each of said chambers are adjacent the lower portions thereof, at least one of said chambers comprising transparent windows adapted and disposed for the transmission of light therethrough and through a body of predetermined thickness of liquid within said chamber between said windows, the improvement in that said open passage comprises a mid-portion between said entrances that is disposed at an elevation sufficiently above said entrances whereby a body of aqueous liquid of substantial depth may be disposed in each of said chambers separated from liquid in the other chamber when the liquid level in said chambers is substantially above the level of said entrances of said open passage into the respective chambers but is lower than the elevation of said mid-portion of said passage and whereby liquid in one of said chambers while so disposed may be forced upon the application of pressure to the surface thereof through said open passage into the other chamber for becoming commingled with liquid in said other chamber.

12. A disposable reaction container according to claim 11 wherein the entrance of said open passage into at least one of said chambers is substantially flush with the bottom of said chamber.

13. A disposable reaction container according to claim 11 wherein the entrance of said open passage into each of said chambers is substantially flush with the bottom thereof.

14. In a disposable reaction container which is composed of rigid or semi-rigid material and which comprises two upstanding chambers laterally disposed with respect to each other and separated from each other by dividing means that is impervious except for an open passage of restricted cross section through said dividing means, at least one of said chambers having transparent windows therein for the transmission of light therethrough and through a body of given thickness of liquid within said chamber between said windows, the improvement in that the entrances of said open passage into each of said chambers is adjacent the bottom thereof and in that the configuration of the inner surface of said passage is effective to entrap a body of air in said passage upon the introduction of aqueous liquids respectively into said chambers to levels that are respectively above the levels of said entrances of said open passage into said chambers and thereby maintain said aqueous liquids separated from each other by said body of entrapped air except when pressure is applied to the surface of liquid in one of said chambers to force liquid from said chamber through said open passage into the other chamber.