CN209475256U - A kind of dialyzate high-efficient purification regenerative system - Google Patents
A kind of dialyzate high-efficient purification regenerative system Download PDFInfo
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- CN209475256U CN209475256U CN201820915670.XU CN201820915670U CN209475256U CN 209475256 U CN209475256 U CN 209475256U CN 201820915670 U CN201820915670 U CN 201820915670U CN 209475256 U CN209475256 U CN 209475256U
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- dialyzate
- efficient purification
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Abstract
The utility model relates to a kind of dialyzate high-efficient purification regenerative systems, the system carries out concentration containing the dialyzate of toxin and waste product to what is come out from dialyzer using ultrafilter, the lean solution that ultrafilter generates is fed directly to dialysis liquid storage tank, concentration rich solution rich in toxin and waste product is sent into dialysis liquid storage tank after absorber carries out adsorption cleaning processing, regenerating unit regenerates the adsorbent in absorber, to achieve the purpose that improve dialyzate cleansing and recycling efficiency, economy, social effect are huge.
Description
Technical field
The utility model relates to it is a kind of using ultrafilter, adsorption cleaning, regenerative combination technology dialyzate high-efficient purification again
Raw system, belongs to apparatus for purifying blood technical field.
Background technique
Haemodialysis is a kind of external dialysis treatment for filtering toxin from the blood of patient using haemodialysis control unit.At present
Most of haemodialysis control units generally comprise computer, fluid pump, blood lines, dialysate lines, dialyzer and for discharging
The tapping line of dialysis solution.It connect the circulatory system of patient with haemodialysis control unit by conduit or fistula needle, and by patient
Blood be continuously pumped through haemodialysis control unit.Blood passes through the dialyzer comprising semi-permeable membrane in haemodialysis control unit.Half
Permeable membrane separates the blood of side and the dialysis solution at another layer.Dialyzer removes waste, toxin and excessive from blood
Water, purified blood return to human body.Waste product and toxin are transferred in dialysis solution by semi-permeable membrane from blood, and single is saturating
Dialyzate about 90-120 liter used in analysis processing discharges after then directly abandoning or handle.Obviously, a large amount of used dialysis
Liquid will increase the cost of dialysis.The object being introduced into blood flow due to the needs that dialyzate can also include various concentration by diffusion
Matter, such as drug, glucose, when these components pass through dialyzer can not completely into blood, thus also can some with useless
The dialyzate of abandoning is discharged;In addition, there are also the beneficial components of some pairs of human bodies to enter discarded dialyzate by semi-permeable membrane in blood.
Above-mentioned various factors causes the increased costs of haemodialysis, waste to increase, and also can cause environmental pollution.Therefore, it produces not
Few dialyzate recovery and utilization technology, typical technology are as follows:
A kind of dialysate regeneration system for portable human dialysis of Chemica Technologies Inc., U.S. application, in
State's number of patent application is 200480038117.3, and the request for data of PCT application is PCT/US2004/043546
(2004.12.22) was authorized, Authorization Notice No. CN1897993B, core technology flow diagram on February 08th, 2012
As shown in Fig. 1.The key technology of the patent uses a kind of dialysate regeneration room 14, can selectively retain toxin and repel
The toxin trap of the cation of selection, wherein the ion selection urase that the toxin trap includes ion selection barrier is fixed
Activated carbon fiber.The advantages of technology is that process is simple, structurally reasonable, easy to carry.But it also has the shortcomings that certain: due into
It is big to enter the low thus required adsorbent adsorption area of toxin concentration in the dialyzate of dialysate regeneration room, the suction of unit volume
Attached dose of adsorption efficiency is lower, and adsorbent inventory is more.
Chinese patent (application number: 201510106383.5) provides a kind of dialysate regeneration device, using reverse osmosis group
Part and electric catalysis reactor based on BDD electrode utilize the very wide potential window of the electric catalysis reactor based on BDD electrode and low
Adsorption capacity, oxidation process is very efficient, effectively can convert and remove waste product and toxin in dialyzate, device it is continuous
Runnability is good.But its also have the shortcomings that it is certain, if electric catalysis reactor may following components generate catalytic action, cause to become
Property or generate the substance that is harmful to the human body, such as penetrate the blood of human body Hubeiwan of dialyzate, be not fully utilized in dialyzate
Needs pass through the substance (such as drug or glucose) that is introduced into blood of diffusion.
(application number: 201710823579.5) providing a kind of device applied to haemodialysis to Chinese patent, typical
Flow chart is as shown in Fig. 2.The device is using the adsorbent for including specific adsorption material and/or non-specific adsorption material
The system and method for the dialysate regeneration that the fluid purification component of box body and reverse osmosis film water purification technique combines.Wherein, it inhales
Specific adsorption material in attached dose of box body becomes in absorption without any chemistry mainly for the absorption of urea in dialysis liquid
Change, the accumulation of any ion will not be generated;Non-specific adsorption material in adsorbent box body is for micro in dialysis liquid
The removal of the substances such as metal ion, kreatinin, β 2M uric acid, micro-content organism.After dialysis liquid removes impurity by adsorbent box body
Following cycle is carried out after influent purification assembly is further purified by reverse osmosis membrane again.The advantages of technology is can be very big
Cost is reduced, is conserved water, and is portable small and exquisite, can meet patient simultaneously the hospital and family the needs of.But it also has centainly
The shortcomings that, i.e., by the dialyzate of adsorbent box body when passing through the fluid purification component of reverse osmosis film water purification technique, formed
Lean solution two parts based on rich solution and pure water rich in macromolecular substances, rich solution are discharged as waste, need in the process periodically
Or continuous moisturizing;It needs dialyzate constituent adjustment system that processing is adjusted by the reuse dialyzate of fluid purification component, adjusts
Section process is extremely complex.
Therefore how to solve the problems, such as above-mentioned technology, a kind of dialysate regeneration system of efficient absorption purification is provided
System, becomes one of hot subject of the area research.
Utility model content
The utility model is in order to solve the problems existing in the prior art, to provide a kind of using ultrafilter, adsorption cleaning and again
The dialyzate high-efficient purification regenerative system of raw combination technique, the system use ultrafilter to being come out from dialyzer containing toxic first
The dialyzate of element and waste product carries out concentration, and the lean solution that ultrafilter generates is fed directly to dialysis liquid storage tank, rich in toxin and
The concentration rich solution of waste product is sent into dialysis liquid storage tank after absorber carries out adsorption cleaning processing, and regenerating unit carries out absorber
Regeneration, to achieve the purpose that improve dialyzate cleansing and recycling efficiency.
The purpose of this utility model is realized by following measures:
A kind of dialyzate high-efficient purification regenerative system, it is characterised in that:
The dialyzate high-efficient purification regenerative system includes ultrafilter 7, absorber 9 and regenerating unit;From dialyzer 2
The dialyzate that middle dialysis fluid side 2-2 comes out is sent into ultrafilter 7 through dialyzate outlet line 6, generation containing blood waste product and
The rich solution of toxin is sent into absorber 9, dialysis liquid storage tank 10 through rich solution outlet pipeline 8, and another part is through lean solution outlet line 11
It is sent into dialysis liquid storage tank 10, the dialyzate in liquid storage tank 10 of dialysing is sent into dialyzer through dialyzate circulating pump 4, dialysate lines 5
2, to form dialyzate cleansing and recycling process;The regenerating unit refers to the regenerated liquid warp come out from regeneration liquid storage tank 12
Regenerated liquid circulating pump 13, regenerated liquid inlet line 14, the first absorber 9-1 or the second absorber 9-2, regenerated liquid outlet line
15, regeneration liquid storage tank 12 is returned to, to form regenerating unit cyclic process.
The dialyzer 2 includes shell, blood side 2-1, semipermeable membrane, dialysis fluid side 2-2, and blood is through dialyzer blood
Suction line 1, the blood side 2-1 of dialyzer 2, dialyzer blood outlet tube line 3 return to human vas.
The ultrafilter 7 includes shell, rich solution side 7-1, ultrafiltration membrane, lean solution side 7-2.
The absorber 9 is provided with adsorbent.
The adsorbent includes specific adsorption material and/or non-specific adsorption material.
The specific adsorption material includes but is not limited to beta-cyclodextrin, the compound of beta-cyclodextrin group, β-ring paste
The modified compound of compound, beta-cyclodextrin chemical modification after essence crosslinking, beta-cyclodextrin are through the modified chemical combination of chemical modification
The high molecular material that object is polymerized, the n-alkyl chain group containing 6 carbon or more compound in any one or it
Between arbitrary proportion combination.
The non-specific adsorption material includes at least active carbon, any one or appointing between them in molecular sieve
The combination of meaning ratio.
The adsorbent is for adsorbing urea nitrogen.
The adsorbent is for adsorbing creatinine.
The adsorbent is for adsorbing phosphate.
The regenerating unit alternately decomposes again the toxin adsorbed in the first absorber 9-1, the second absorber 9-2
Raw, the first absorber 9-1, the second absorber 9-2 alternately put into operation, regenerate.
Semipermeable membrane in the dialyzer 2 for separating blood waste product and toxin, including but not limited to urea nitrogen,
Creatinine and other small organic human waste molecules, water.
The unaccounted technical characteristic of the utility model is carried out mating using the mature prior art.
The utility model has the advantages that compared with prior art
1, this dialyzate high-efficient purification regenerative system is in ultrafilter, absorber bringing normally into operation, operational process zero-emission;
2, the substance such as drug, glucose etc. that the various needs being incorporated in dialyzate are introduced into blood flow by diffusion, can
Circulation efficiently utilizes, and reduces to the pollution of environment;
3, many small-molecule substances beneficial to human body for entering dialyzate from blood penetration are recycled in dialyzate to one
When determining concentration, it is based on concentration difference, overall seepage discharge effectively reduces;
4, the toxin adsorbance of the identical adsorption area of identical adsorbent obviously increases, and adsorption efficiency is high, is dissolved in lean solution
The soluble small molecular material beneficial to human body do not contacted with adsorbent, will not generate it is rotten, be diffused into blood generate danger
Harmful probability is effectively reduced.
Detailed description of the invention
Fig. 1 is a kind of dialysate regeneration system flow diagram (Chinese Patent Application No. for portable human dialysis
For 200480038117.3).
Fig. 2 is that (Chinese Patent Application No. is for a kind of device flow diagram applied to haemodialysis
201710823579.5)。
A kind of dialyzate high-efficient purification regenerative system flow diagram of Fig. 3 the utility model.
In Fig. 3: 1- dialyzer blood inlet line;2- dialyzer;2-1- blood side;2-2- dialysis fluid side;3- dialyzer
Blood outlet tube line;4- dialyzate circulating pump;5- dialysate lines;6- dialyzate outlet line;7- ultrafilter;7-1- rich solution
Side;7-2- lean solution side;8- rich solution outlet pipeline;The first absorber of 9-1-;The second absorber of 9-2-;10- dialysis liquid storage tank;11-
Lean solution outlet line;12- regenerates liquid storage tank;13- regenerated liquid circulating pump;14- regenerated liquid inlet line;15- regenerated liquid outlet
Line.
Specific embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.
Embodiment 1:
As shown in figure 3, a kind of dialyzate high-efficient purification regenerative system that embodiment uses:
The dialyzate high-efficient purification regenerative system includes ultrafilter 7, absorber 9 and regenerating unit;From dialyzer 2
The dialyzate that middle dialysis fluid side 2-2 comes out is sent into ultrafilter 7 through dialyzate outlet line 6, generation containing blood waste product and
The rich solution of toxin is sent into absorber 9, dialysis liquid storage tank 10 through rich solution outlet pipeline 8, and another part is through lean solution outlet line 11
It is sent into dialysis liquid storage tank 10, the dialyzate in liquid storage tank 10 of dialysing is sent into dialyzer through dialyzate circulating pump 4, dialysate lines 5
2, to form dialyzate cleansing and recycling process;The regenerating unit refers to the regenerated liquid warp come out from regeneration liquid storage tank 12
Regenerated liquid circulating pump 13, regenerated liquid inlet line 14, the first absorber 9-1 or the second absorber 9-2, regenerated liquid outlet line
15, regeneration liquid storage tank 12 is returned to, to form regenerating unit cyclic process.
The dialyzer 2 includes shell, blood side 2-1, semipermeable membrane, dialysis fluid side 2-2, and blood is through dialyzer blood
Suction line 1, the blood side 2-1 of dialyzer 2, dialyzer blood outlet tube line 3 return to human vas.
The ultrafilter 7 includes shell, rich solution side 7-1, ultrafiltration membrane, lean solution side 7-2.
The absorber 9 is provided with adsorbent.
The adsorbent includes specific adsorption material and non-specific adsorption material.
The specific adsorption material include beta-cyclodextrin, the compound of beta-cyclodextrin group, beta-cyclodextrin crosslinking after
Compound, the modified compound of beta-cyclodextrin chemical modification, beta-cyclodextrin through the modified compound polymerization of chemical modification and
At high molecular material, n-alkyl chain group containing 6 carbon or more compound in any one or they between
Arbitrary proportion combination.
The non-specific adsorption material includes at least active carbon, any one in molecular sieve.
The adsorbent is for adsorbing urea nitrogen.
The adsorbent is for adsorbing creatinine.
The adsorbent is for adsorbing phosphate.
The regenerating unit alternately decomposes again the toxin adsorbed in the first absorber 9-1, the second absorber 9-2
Raw, the first absorber 9-1, the second absorber 9-2 intersection put into operation, regenerate.
Semipermeable membrane in the dialyzer 2 for separating blood waste product and toxin, including but not limited to urea nitrogen,
Creatinine and other small organic human waste molecules, water.
The unaccounted technical characteristic of the utility model is carried out mating using the mature prior art.
Although the utility model has been described by way of example and in terms of the preferred embodiments, they be not for limiting the utility model,
It is any to be familiar with this field technical professional, in the spirit and scope for not departing from the utility model, it can make various simply to repair
Change, equivalent variations, still falls within the protection scope of technical solutions of the utility model.
Claims (9)
1. a kind of dialyzate high-efficient purification regenerative system, it is characterised in that:
The dialyzate high-efficient purification regenerative system includes ultrafilter (7), absorber (9) and regenerating unit;From dialyzer (2)
The dialyzate that middle dialysis fluid side (2-2) comes out is sent into ultrafilter (7) through dialyzate outlet line (6), and generation is given up containing blood
The rich solution of product and toxin is sent into absorber (9), dialysis liquid storage tank (10) through rich solution outlet pipeline (8), and another part is through lean solution
Outlet line (11) is sent into dialysis liquid storage tank (10), and the dialyzate in dialysis liquid storage tank (10) is through dialyzate circulating pump (4), dialysis
Liquid pipe line (5) is sent into dialyzer (2), to form dialyzate cleansing and recycling process;The regenerating unit refers to from regenerated liquid
The regenerated liquid that storage tank (12) comes out is through regenerated liquid circulating pump (13), regenerated liquid inlet line (14), the first absorber (9-1) or the
Two absorbers (9-2), regenerated liquid outlet line (15) return to regeneration liquid storage tank (12), to form regenerating unit cyclic process.
2. dialyzate high-efficient purification regenerative system according to claim 1, it is characterised in that:
The dialyzer (2) includes shell, blood side (2-1), semipermeable membrane, dialysis fluid side (2-2);Blood is through dialyzer blood
Liquid suction line (1), the blood side (2-1) of dialyzer (2), dialyzer blood outlet tube line (3) return to human vas.
3. dialyzate high-efficient purification regenerative system according to claim 1, it is characterised in that:
The ultrafilter (7) includes shell, rich solution side (7-1), ultrafiltration membrane, lean solution side (7-2).
4. dialyzate high-efficient purification regenerative system according to claim 1, it is characterised in that:
First absorber (9-1) or the second absorber (9-2) is provided with adsorbent;The adsorbent includes specificity
Adsorbent material and/or non-specific adsorption material.
5. dialyzate high-efficient purification regenerative system according to claim 4, it is characterised in that:
The adsorbent is for adsorbing urea nitrogen.
6. dialyzate high-efficient purification regenerative system according to claim 4, it is characterised in that:
The adsorbent is for adsorbing creatinine.
7. dialyzate high-efficient purification regenerative system according to claim 4, it is characterised in that:
The adsorbent is for adsorbing phosphate.
8. dialyzate high-efficient purification regenerative system according to claim 4, it is characterised in that:
The specific adsorption material includes the change after beta-cyclodextrin, the compound of beta-cyclodextrin group, beta-cyclodextrin crosslinking
Close object, compound, the beta-cyclodextrin that beta-cyclodextrin chemical modification is modified are polymerized through the modified compound of chemical modification
High molecular material, n-alkyl chain group containing six carbon or more compound in any one or it is any between them
Ratio combination.
9. dialyzate high-efficient purification regenerative system according to claim 4, it is characterised in that:
The non-specific adsorption material includes active carbon, any one or the arbitrary proportion group between them in molecular sieve
It closes.
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CN108785773A (en) * | 2018-06-13 | 2018-11-13 | 上海健康医学院 | A kind of dialyzate high-efficient purification regenerative system |
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CN108785773A (en) * | 2018-06-13 | 2018-11-13 | 上海健康医学院 | A kind of dialyzate high-efficient purification regenerative system |
CN108785773B (en) * | 2018-06-13 | 2024-04-09 | 上海健康医学院 | Efficient purifying and regenerating system for dialysate |
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