CN206223510U - Ion exchange resin sample pretreatment or preparation facilities - Google Patents

Ion exchange resin sample pretreatment or preparation facilities Download PDF

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Publication number
CN206223510U
CN206223510U CN201621310393.7U CN201621310393U CN206223510U CN 206223510 U CN206223510 U CN 206223510U CN 201621310393 U CN201621310393 U CN 201621310393U CN 206223510 U CN206223510 U CN 206223510U
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CN
China
Prior art keywords
valve
exchange column
lucite
resin
exhaust
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Active
Application number
CN201621310393.7U
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Chinese (zh)
Inventor
张建新
周诗宇
李勐
孙冬冬
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Electric Power Research Institute of State Grid Jilin Electric Power Co Ltd
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Electric Power Research Institute of State Grid Jilin Electric Power Co Ltd
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Priority to CN201621310393.7U priority Critical patent/CN206223510U/en
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Abstract

The utility model is related to a kind of ion exchange resin sample pretreatment or preparation facilities, belongs to ion exchange resin treatment or preparation facilities.Four kinds of solvent buckets are connected through valve with the pump line of two peristaltic pumps respectively, two pump lines of peristaltic pump are connected with two groups of positive resin lucite exchange columns and negative resin lucite exchange column respectively, and four inverted U water level limit for height pipes are connected with each positive resin lucite exchange column and negative resin lucite exchange column respectively.Advantage is structure novel, and by combining pretreatment or preparation that four solvent buckets, two positive resin lucite exchange columns, two negative resin lucite exchange columns can complete to the two kinds of resin of yin, yang, operation is clear convenient, efficiency high.

Description

Ion exchange resin sample pretreatment or preparation facilities
Technical field
The utility model belongs to ion exchange resin treatment or preparation facilities.
Background technology
The acceptance test of the various spherical ion exchange resin of thermal power generation station-service will be set according to DL/T519 resins acceptance criteria Fat is divided into 4 types, and the pretreatment before every kind of resin analysis is prepared and is divided into 4 steps, and each step is as needed on resin By the solution or pure water of constant density, every kind of resin preprocessing process and Sample Preparation Procedure do not calculate dressing working time need Want 220 minutes(Positive resin)Or 260 minutes(Negative resin)More than, Artificial sample pretreatment and prepare without special device, respectively From each treatment is completed, cause the complicated workload of work big, when resin sample amount is big, treatment effeciency is low can not to be met resin and test Acceptance test works.
The content of the invention
The utility model provides a kind of ion exchange resin sample pretreatment or preparation facilities, to solve current Artificial sample The complicated workload that worked present in pretreatment and preparation is big, the low problem for the treatment of effeciency.
The utility model is adopted the technical scheme that:HCL solvents bucket is connected with valve one and valve two respectively, NaOH Solvent bucket is connected with valve three and valve four respectively, and NaCl solvents bucket is connected with valve five and valve six respectively, pure Water bucket is connected with valve seven and valve eight respectively, wherein after valve one, valve three, valve five and the parallel connection of valve seven respectively with The pump line one and pump line two of peristaltic pump one are connected, and positive resin lucite exchange column one is connected with pump line one, the organic glass of positive resin Glass exchange column two is connected with pump line two, wherein after valve two, valve four, valve six and the parallel connection of valve eight respectively with peristaltic pump two Pump line three and pump line four are connected, and negative resin lucite exchange column one is connected with pump line three, negative resin lucite exchange column two Be connected with pump line two, exhaust-valve one, exhaust-valve two, exhaust-valve three and exhaust-valve four respectively with positive resin lucite exchange column First, positive resin lucite exchange column two, negative resin lucite exchange column one and the lower section of negative resin lucite exchange column two Pipeline is connected, the pipeline connection between inverted U water level limit for height Guan Yiyu exhaust-valves one and positive resin lucite exchange column one, U Pipeline connection between type water level limit for height Guan Eryu exhaust-valves two and positive resin lucite exchange column two, inverted U water level limit for height pipe Pipeline connection between three and exhaust-valve three and negative resin lucite exchange column three, inverted U water level limit for height Guan Siyu exhaust-valves four And the pipeline connection between negative resin lucite exchange column four.
The utility model has the advantages that structure is novel, by combining four solvent buckets, two positive resin lucite Exchange column, two negative resin lucite exchange columns can complete the pretreatment or preparation to the two kinds of resin of yin, yang, operation It is clear convenient, efficiency high.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
HCL solvents bucket 1 is connected with valve 1 and valve 2 20 respectively, NaOH solvents bucket 2 respectively with valve 3 21 and valve 4 22 connect, NaCl solvents bucket 3 is connected with valve 5 23 and valve 6 24 respectively, 4 points of pure water bucket Be not connected with valve 7 25 and valve 8 26, wherein after valve one, valve three, valve five and the parallel connection of valve seven respectively with peristaltic pump One 5 pump line 1 and pump line 2 502 connection, positive resin lucite exchange column 1 is connected with pump line 1, and positive resin has Machine glass exchange column 27 is connected with pump line 2 502, wherein after valve two, valve four, valve six and the parallel connection of valve eight respectively with it is compacted The pump line 3 801 and pump line 4 802 of dynamic pump 28 are connected, and negative resin lucite exchange column 1 is connected with pump line 3 801, the moon tree Fat lucite exchange column 2 10 is connected with pump line 2 802, exhaust-valve 1, exhaust-valve 2 16, exhaust-valve 3 17 and exhaust-valve 4 18 exchange with positive resin lucite exchange column one, positive resin lucite exchange column two, negative resin lucite respectively Post one and the lower section pipeline connection of negative resin lucite exchange column two, inverted U water level limit for height pipe 1 and exhaust-valve 1 and sun Pipeline connection between resin lucite exchange column one, inverted U water level limit for height pipe 2 12 is organic with exhaust-valve 2 16 and positive resin Pipeline connection between glass exchange column two, inverted U water level limit for height pipe 3 13 is exchanged with exhaust-valve 3 17 and negative resin lucite Pipeline connection between post three, between inverted U water level limit for height pipe 4 14 and exhaust-valve 4 18 and negative resin lucite exchange column four Pipeline is connected.

Claims (1)

1. a kind of ion exchange resin sample pretreatment or preparation facilities, it is characterised in that:HCL solvents bucket respectively with valve One and valve two connect, NaOH solvents bucket is connected with valve three and valve four respectively, NaCl solvents bucket respectively with valve Door five and valve six are connected, and pure water bucket is connected with valve seven and valve eight respectively, wherein valve one, valve three, valve five It is connected with the pump line one and pump line two after the parallel connection of valve seven respectively with peristaltic pump one, positive resin lucite exchange column one and pump line One connection, positive resin lucite exchange column two is connected with pump line two, and wherein valve two, valve four, valve six and valve eight be simultaneously Pump line three and pump line four after connection respectively with peristaltic pump two are connected, and negative resin lucite exchange column one is connected with pump line three, cloudy Resin lucite exchange column two is connected with pump line two, exhaust-valve one, exhaust-valve two, exhaust-valve three and exhaust-valve four respectively with sun Resin lucite exchange column one, positive resin lucite exchange column two, negative resin lucite exchange column one and negative resin have The lower section pipeline connection of machine glass exchange column two, inverted U water level limit for height Guan Yiyu exhaust-valves one and positive resin lucite exchange column Pipeline connection between one, the pipeline between inverted U water level limit for height Guan Eryu exhaust-valves two and positive resin lucite exchange column two connects Connect, the pipeline connection between inverted U water level limit for height Guan Sanyu exhaust-valves three and negative resin lucite exchange column three, inverted U water level Pipeline connection between limit for height Guan Siyu exhaust-valves four and negative resin lucite exchange column four.
CN201621310393.7U 2016-12-01 2016-12-01 Ion exchange resin sample pretreatment or preparation facilities Active CN206223510U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621310393.7U CN206223510U (en) 2016-12-01 2016-12-01 Ion exchange resin sample pretreatment or preparation facilities

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621310393.7U CN206223510U (en) 2016-12-01 2016-12-01 Ion exchange resin sample pretreatment or preparation facilities

Publications (1)

Publication Number Publication Date
CN206223510U true CN206223510U (en) 2017-06-06

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621310393.7U Active CN206223510U (en) 2016-12-01 2016-12-01 Ion exchange resin sample pretreatment or preparation facilities

Country Status (1)

Country Link
CN (1) CN206223510U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113083379A (en) * 2021-03-15 2021-07-09 华电电力科学研究院有限公司 Full-automatic ion exchange resin pretreatment device for laboratory

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113083379A (en) * 2021-03-15 2021-07-09 华电电力科学研究院有限公司 Full-automatic ion exchange resin pretreatment device for laboratory

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