CN202185179U - Grouped resin adsorption unit - Google Patents

Grouped resin adsorption unit Download PDF

Info

Publication number
CN202185179U
CN202185179U CN2011203248195U CN201120324819U CN202185179U CN 202185179 U CN202185179 U CN 202185179U CN 2011203248195 U CN2011203248195 U CN 2011203248195U CN 201120324819 U CN201120324819 U CN 201120324819U CN 202185179 U CN202185179 U CN 202185179U
Authority
CN
China
Prior art keywords
resin adsorption
tower
pipe
storage tank
adsorption unit
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011203248195U
Other languages
Chinese (zh)
Inventor
刘培保
叶春穗
章魁文
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WENZHOU CHINZ MACHINERY CO Ltd
Original Assignee
WENZHOU CHINZ MACHINERY CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by WENZHOU CHINZ MACHINERY CO Ltd filed Critical WENZHOU CHINZ MACHINERY CO Ltd
Priority to CN2011203248195U priority Critical patent/CN202185179U/en
Application granted granted Critical
Publication of CN202185179U publication Critical patent/CN202185179U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

The utility model discloses a grouped resin adsorption unit, comprising a plurality of resin absorption and separation columns. Every two resin absorption and separation columns belong to one absorber combination. Each absorber combination further comprises a storage tank and an upstream conveying pipe. The upstream conveying pipe is provided with a pump. The upper end of the upstream conveying pipe is connected with the lower end of the storage tank and connected with a feed branch pipe through a pipeline system. The feed branch pipe is connected with a feed header pipe and the storage tank is connected with the upper ends of the absorption and separation columns respectively through guide pipes. The grouped resin adsorption unit further comprises an end product liquid or liquid waste downstream collecting heater pipe, an end product liquid upstream collecting header pipe and a vacuumizing pipe. The downstream collecting heater pipe is respectively is communicated with the pipeline system at the lower ends of the absorber combinations and the upper collecting heater pipe is respectively communicated with the storage tank in the absorber combination. The vacuumizing pipe is respectively communicated with the upper ends of the absorption and separation columns. Valves for controlling on-off of the pipeline are installed in each pipeline. The grouped resin adsorption unit has high work efficiency, good continuity and can realize staged, layered and effective consistent operations by filling different resins.

Description

Packet type resin adsorption unit
Technical field
The utility model relates to a kind of packet type resin adsorption unit, and it is mainly used in resin adsorption.
Background technology
The absorption of tradition fat generally includes only single resin adsorption splitter; For abundant polymeric adsorbent; The feed liquid that often needs to pass through resin particle absorption is re-entered subjob again in the resin adsorption splitter; Therefore the continuity of working is relatively poor, be difficult to tackle large batch of feed liquid and handle, and can't realize stage by stage, by different level, the coherent operation of branch active ingredient.
Summary of the invention
The utility model technical problem to be solved provides a kind of packet type resin adsorption unit; High efficiency, the continuity of this packet type resin adsorption unit are better, and can realize stage by stage through the different resin of filling, by different level, divide the coherent operation of active ingredient.
For this reason, the packet type resin adsorption unit that the utility model provides comprises a plurality of resin adsorption splitters; Per two resin adsorption splitters belong to an adsorbent equipment combination; Each adsorbent equipment combination also comprises storage tank and up carrier pipe, and up carrier pipe disposes pump, and up carrier pipe upper end connects the storage tank lower end and is in charge of through pipe-line system connection charging; Charging is in charge of and is connected the charging house steward, and storage tank connects through conduit respectively with resin adsorption splitter upper end; Packet type resin adsorption unit also comprises finished fluid or the descending collection of waste liquid house steward, finished fluid up collection house steward and vacuum-pumping tube; Descending collection house steward makes up the pipe-line system conducting of lower end respectively with each adsorbent equipment; Storage tank conducting during up collection house steward makes up with each adsorbent equipment respectively; Vacuum-pumping tube respectively with the upper end conducting of each resin adsorption splitter, be separately installed with the valve that is used for the control piper break-make in each pipeline.
Because the packet type resin adsorption unit that the utility model provides disposes the combination of many group adsorbent equipments; Comprise two resin adsorption splitters in every group of adsorbent equipment combination, realize respectively organizing the series connection between the adsorbent equipment and being connected in parallel, be connected in series and realize the continuous adsorption treatment of feed liquid through pipeline connection between each group adsorbent equipment combination and valve control; Resinous principle is adsorbed more fully; And be connected in parallel the bigger feed liquid of total amount can be processed simultaneously, thereby increase work efficiency, can also carry out forward and reverse circulation absorption in addition; Make resin be in poised state all the time; Can avoid resin to load phenomenons such as the wall stream uneven, that one-way flow causes, channel, dried awl, make resin adsorption more even, be used to adsorb the resin particle of feed liquid to greatest extent.
Description of drawings
The structural representation of the packet type resin adsorption unit that Fig. 1 provides for the utility model.
Fig. 2 is the structural representation of the resin adsorption splitter among Fig. 1.
The specific embodiment
As shown in Figure 1; The packet type resin adsorption unit that the utility model provides comprises a plurality of resin adsorption splitters 1; Per two resin adsorption splitters 1 belong to an adsorbent equipment combination, dispose three adsorbent equipment combinations altogether, and each adsorbent equipment combination also comprises storage tank 2 and up carrier pipe 3; Up carrier pipe 3 disposes pump 4; Up carrier pipe 3 upper ends connect storage tank 2 lower ends and are in charge of 5 through pipe-line system 10 connection chargings, and charging is in charge of 5 and is connected charging house stewards 6, and storage tank 2 connects through conduit respectively with resin adsorption splitter 1 upper end; Packet type resin adsorption unit also comprises finished fluid or the descending collection of waste liquid house steward 7, the up collection of finished fluid house steward 8 and vacuum-pumping tube 9; Descending collection house steward 7 makes up pipe-line system 10 conductings of lower end respectively with each adsorbent equipment; Storage tank 2 conductings during up collection house steward 8 makes up with each adsorbent equipment respectively; Vacuum-pumping tube 9 respectively with each resin adsorption splitter 1 upper end conducting, be separately installed with the valve that is used for the control piper break-make in each pipeline.
As shown in Figure 2; In the above-described embodiments, resin adsorption splitter 1 comprises tower body 11, and tower body 11 two ends are connected with end socket 12 through flange apparatus respectively; The end socket 12 at tower body 11 two ends and the flange connections between the tower body 11 are provided with filter screen; Tower body 11 tops configuration resin inlet 18, tower body 1 bottom configuration resin outlet 19 is provided with the heat exchange coil 13 that spiral distributes in the tower body 11; Heat exchange coil has the hot and cold water inlets 14 and hot and cold waters outlet 15 that extend outside the tower body 11 respectively in two ends about in the of 13; Also vertically be distributed with the resin adsorption body that adopts resin to process in the tower body 11, the resin adsorption body is the particulate resins that is arranged in the tower body 11, and particulate resins is covered with the space of tower body 75%-80%.
As shown in Figure 1; Several kinds of operating processes that following illustrated in detail feed liquid is handled: the use of first kind of operation, an adsorbent equipment combination; At first feed liquid gets into from charging house steward 6, be in charge of 5 through charging then and get into pipe-line systems 10, feed liquid get into pipe-line system 10 backs through valve controlling flow to making it flow into up carrier pipe 3; Pump 4 through on the up carrier pipe 3 is transported to storage tank 2 with feed liquid; Feed liquid in the storage tank 2 is transported to respectively in two resin adsorption splitters 1 through conduit again, and configuration valve control feed liquid is mobile on the conduit, enters finished fluid or the descending collection of waste liquid house steward 7 from the lower end through pipe-line system 10 after the adsorption treatment of feed liquid through resin adsorption splitter 1; To making it flow into descending collection house steward 7, descending collection house steward 7 discharges waste liquid through valve controlling flow in feed liquid entering pipe-line system 10 backs.The storage tank 2 back unifications that second kind of operation, several kinds of adsorbent equipment combination carrying out parallel connections, the feed liquid after the resin adsorption splitter 1 in each adsorbent equipment combination all will separate are collected separately are transported to the up collection of finished fluid house steward 8.The third operation, first kind of mode of operation and second kind of mode of operation are carried out contrary operation and also can be carried out resin adsorption.The 4th kind of operation, three groups of adsorbent equipments combinations are connected (can carry out adsorption operations of the same race; Also can adorn different resins; Operate stage by stage), feed liquid is through unified the collecting in the storage tank 2 in resin adsorption splitter 1 back in first adsorbent equipment combination, again through conduit and valve control; Feed liquid is transported to second resin adsorption splitter 1 in the adsorbent equipment combination once more, and (this moment, feed liquid got into from resin adsorption splitter 1 upper end; Discharge the lower end), the resin adsorption splitter 1 in then through pipe-line system 10 feed liquid being made up through three adsorbent equipments of catheter guidance to the is again discharged through the up collection of finished fluid house steward 8 at last.

Claims (4)

1. packet type resin adsorption unit; It is characterized in that: comprise a plurality of resin adsorption splitters (1); Per two resin adsorption splitters (1) belong to an adsorbent equipment combination; Each adsorbent equipment combination also comprises storage tank (2) and up carrier pipe (3), and up carrier pipe (3) disposes pump (4), and up carrier pipe (3) upper end connects storage tank (2) lower end and is in charge of (5) through pipe-line system (10) connection charging; Charging is in charge of (5) and is connected charging house steward (6), and storage tank (2) connects through conduit respectively with resin adsorption splitter (1) upper end; Said packet type resin adsorption unit also comprises finished fluid or the descending collection of waste liquid house steward (7), the up collection of finished fluid house steward (8) and vacuum-pumping tube (9); Descending collection house steward (7) makes up pipe-line system (10) conducting of lower end respectively with each adsorbent equipment; Storage tank (2) conducting during up collection house steward (8) makes up with each adsorbent equipment respectively; Vacuum-pumping tube (9) respectively with the upper end conducting of each resin adsorption splitter (1), be separately installed with the valve that is used for the control piper break-make in each pipeline.
2. packet type resin adsorption unit according to claim 1 is characterized in that: dispose three adsorbent equipment combinations altogether.
3. packet type resin adsorption unit according to claim 1 and 2; It is characterized in that: said resin adsorption splitter (1) comprises tower body (11); Tower body (11) two ends are connected with end socket (12) through flange apparatus respectively; The end socket (12) at tower body (11) two ends and the flange connections between the tower body (11) are provided with filter screen; Tower body (11) top configuration resin inlet (18), tower body (1) bottom configuration resin outlet (19) is provided with the heat exchange coil (13) that spiral distributes in the said tower body (11); Heat exchange coil (13) two ends up and down has the hot and cold water inlet (14) and the hot and cold water outlet (15) of extending outside the tower body (11) respectively, also vertically is distributed with the resin adsorption body that adopts resin to process in the tower body (11).
4. packet type resin adsorption unit according to claim 3 is characterized in that: said resin adsorption body is for to be arranged at the particulate resins in the tower body (11), and particulate resins is covered with the space of tower body 75%-80%.
CN2011203248195U 2011-08-25 2011-08-25 Grouped resin adsorption unit Expired - Fee Related CN202185179U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203248195U CN202185179U (en) 2011-08-25 2011-08-25 Grouped resin adsorption unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203248195U CN202185179U (en) 2011-08-25 2011-08-25 Grouped resin adsorption unit

Publications (1)

Publication Number Publication Date
CN202185179U true CN202185179U (en) 2012-04-11

Family

ID=45916658

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011203248195U Expired - Fee Related CN202185179U (en) 2011-08-25 2011-08-25 Grouped resin adsorption unit

Country Status (1)

Country Link
CN (1) CN202185179U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103073118A (en) * 2013-02-03 2013-05-01 大连涌清水处理技术有限公司 Parallel-connected continuous adsorption system in wastewater treatment process
CN103877827A (en) * 2014-02-25 2014-06-25 浙江工业大学 Organic waste gas adsorbing recovery device and process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103073118A (en) * 2013-02-03 2013-05-01 大连涌清水处理技术有限公司 Parallel-connected continuous adsorption system in wastewater treatment process
CN103877827A (en) * 2014-02-25 2014-06-25 浙江工业大学 Organic waste gas adsorbing recovery device and process
CN103877827B (en) * 2014-02-25 2016-03-09 浙江工业大学 A kind of organic exhaust gas adsorption retracting device and technique

Similar Documents

Publication Publication Date Title
CN201505465U (en) Continuous extraction separation concentrator
CN202185179U (en) Grouped resin adsorption unit
CN205495287U (en) Propylene recovery's equipment is carried out with pressure swing adsorption method
CN205953707U (en) Solar energy water body pollution purifies ship
CN204607721U (en) Reverse osmosis water treating equipment
CN103073088B (en) Continuous adsorption system for sewage treatment process
CN201610390U (en) Water feeding device of integrated oxygen remover
CN106512705A (en) Biological desulfurization device for flue gas
CN110526384A (en) A kind of high efficiency ozone water apparatus
CN202666547U (en) Automatic control water purification device
CN107726514A (en) A kind of Cycle Unit high-pressure spray humidification device
CN204607723U (en) Reverse osmosis water purifying plant
CN205045843U (en) Active carbon filter
CN204607722U (en) Water treating equipment
CN204607720U (en) Pole low-pressure water treatment facility
CN204910903U (en) Take whirl dirt separator of gas -liquid separation function
CN207959486U (en) A kind of hydraulic engineering water pipe junction cleaning device
CN207865615U (en) A kind of Cycle Unit high-pressure spray humidification device
CN203930451U (en) A kind of continuous processing line factory effluent recovery control device
CN102500231A (en) Novel and high-efficiency equipment for treating waste gas by using biotrickling filter
CN203342496U (en) Wheat pulp filtering device
CN203112546U (en) Continuous adsorption system of sewage treatment process
CN203123690U (en) Fine and efficient pressurizing backlash and recharge filter unit
CN209957508U (en) Reverse osmosis water purification drinking machine system suitable for double water sources
CN202773611U (en) Automatic watering system for potted plants

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
EXPY Termination of patent right or utility model
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120411

Termination date: 20140825