US20060091228A1 - Moisture-absorbing polymer particle, method for forming the same and application thereof - Google Patents

Moisture-absorbing polymer particle, method for forming the same and application thereof Download PDF

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Publication number
US20060091228A1
US20060091228A1 US10/978,374 US97837404A US2006091228A1 US 20060091228 A1 US20060091228 A1 US 20060091228A1 US 97837404 A US97837404 A US 97837404A US 2006091228 A1 US2006091228 A1 US 2006091228A1
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absorbing device
signal
temperature
absorbing
dew point
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US10/978,374
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Keh-Ying Hsu
Chu-Yi Pang
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Chung Yuan Christian University
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Chung Yuan Christian University
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Priority to US10/978,374 priority Critical patent/US20060091228A1/en
Assigned to CHUNG YUAN CHRISTIAN UNIVERSITY reassignment CHUNG YUAN CHRISTIAN UNIVERSITY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HSU, KEH-YING, PANG, CHU-YI
Publication of US20060091228A1 publication Critical patent/US20060091228A1/en
Priority to US12/015,852 priority patent/US20080110998A1/en
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours
    • B01D53/261—Drying gases or vapours by adsorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26—Synthetic macromolecular compounds
    • B01J20/261—Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26—Synthetic macromolecular compounds
    • B01J20/265—Synthetic macromolecular compounds modified or post-treated polymers
    • B01J20/267—Cross-linked polymers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206—Organic carriers, supports or substrates
    • B01J20/3208—Polymeric carriers, supports or substrates
    • B01J20/321—Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3268—Macromolecular compounds
    • B01J20/328—Polymers on the carrier being further modified
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3291—Characterised by the shape of the carrier, the coating or the obtained coated product
    • B01J20/3293—Coatings on a core, the core being particle or fiber shaped, e.g. encapsulated particles, coated fibers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/20—Organic adsorbents
    • B01D2253/202—Polymeric adsorbents

Definitions

  • the present invention is generally related to a polymer particle, and more particularly to a moisture-absorbing polymer particle, a method for forming the same, and applications thereof.
  • a new moisture-absorbing polymer particle is provided. This particle can meet the requirement of low energy consumption and high dehumidifying efficiency.
  • One object of the present invention is to employ the thermo-sensitive properties of PNIPAm for moisture-adsorbing/dehumidifying usage.
  • LCST lower critical solution temperature
  • the PNIPAm copolymer particles are hydrophilic and have a capacity to be swollen several times larger than its original volume.
  • the polymer chains contract and the PNIPAm copolymer particles become hydrophobic and can be rapidly dewatered.
  • the present invention is characterized by the above-mentioned low-regeneration temperature feature and through which the present invention provides a moisture-absorbing polymer particle which can serve as an energy saving dehumidifier at normal room temperature. Therefore, this present invention does have the economic advantages for industrial applications.
  • the present invention discloses a moisture-absorbing polymer particle, which either comprises PNIPAm crosslinking copolymer or a structure having PNIPAm crosslinking copolymer as a core and polymer with sulfonic acid group as a shell.
  • the present invention also discloses a method for producing the provided moisture-absorbing polymer particle and an application thereof; the application is referred to as a continuous dehumidifying system which comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
  • FIG. 1 is a flow chart of a method for forming a moisture-absorbing polymer particle in accordance with a third embodiment of the present invention
  • FIG. 2 is a schematic diagram illustrating a continuous dehumidifying system in accordance with a fourth embodiment of the present invention.
  • FIG. 3 is a schematic diagram illustrating a continuous dehumidifying system in accordance with a fifth embodiment of the present invention.
  • a moisture-absorbing polymer particle which comprises poly-N-isopropylacrylamide (PNIPAm] crosslinking colymer.
  • the crosslinking copolymer is polymerized by N-isopropylacrylamide (NIPAm), as a monomer, with an acrylamide-type crosslinker having at least two double bonds, wherein the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
  • the amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %.
  • a moisture-absorbing polymer particle with a structure of a core, mainly PNIPAm, and a shell comprising polymer with sulfonic acid group.
  • the core comprises PNIPAm crosslinking copolymer and is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds, wherein the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
  • the amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %.
  • the polymer of the shell further comprises [poly(styrene sulfonic acid) PSSA].
  • a method for forming moisture-absorbing polymer particles is provided.
  • a first mixing process 110 is performed to mix NIPAm an acrylamide-type crosslinker having at least two double bonds and water into a first solution 115 , wherein the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
  • the amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %.
  • a dissolving process 120 is performed to dissolve a water-soluble initiator containing ammounium persulfate(APS) into water to form a second solution 125 .
  • the amount of the water-soluble initiator to use is selected0.5 wt %-2 wt % of NIPAm.
  • a second mixing process 130 is performed at a specific temperature to mix the first solution 115 with the second solution 125 to form a third solution 135 , wherein the specific temperature is lower than 33° C.
  • a dispersion process 140 is performed at the specific temperature to uniformly distribute a plurality of liquid drops containing the third solution 135 in an organic solvent containing toluene, so as to form a water-in-oil system.
  • a catalyst containing N,N,N′,N′,-Tetramethylethylendiamine (TEMED) is added into the organic solvent for starting and accelerating a polymerization 150 in the liquid drops, wherein the NIPAm and the acrylamide-type crosslinker are polymerized into a first moisture-absorbing polymer particle 155 A.
  • the first moisture-absorbing particle 155 A is formed under a condition with inert gas purged, and the polymerization time is longer than 4 hours.
  • the provided method for forming moisture-absorbing polymer particles can further comprise at least one purification process 160 and a shell-forming process 170 .
  • the purification process 160 further comprises removing unreacted NIPAm, unreacted acrylamide-type crosslinker and impurities by an extracting agent (such as ketone), and removing the extracting agent by a cleaning agent (such as water).
  • the shell-forming process 170 forms a shell region having sulfonic acid group onto the surface of the previous purifed first moisture-absorbing polymer particle 155 A, and through which to form a second moisture-absorbing polymer particle 155 B.
  • the shell-forming process 170 comprises: coating a 30 wt % [poly(styrene sulfonic acid), PSSA] solution onto the surface of the previous purifed first moisture-absorbing polymer particle 155 A; and performing a drying procedure to form a shell region having PSSA on the previous purifed first moisture-absorbing polymer particle 155 A.
  • a continuous dehumidifying system comprises a first module 200 A to perform a dehumidifying process and a second module 200 B to perform a regeneration process, wherein the first module comprises a plurality of moisture-absorbing polymer particles to process a humid gas stream inlet and generate a dryed exhaust stream outlet; and the second module 200 B processes the used moisture-absorbing polymer particles in the first module 200 A; regenates them and prepares for next dehumidifying process going to perform.
  • the above mentioned moisture-absorbing polymer particles comprises poly-N-isopropylacrylamide (PNIPAm] crosslinking copolymer which is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds.
  • the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
  • the amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %.
  • the moisture-absorbing polymer particle can have a shell which is made of a material having sulfonic acid group, such as [poly(styrene sulfonic acid), PSSA].
  • the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
  • the first module 200 A further comprises a first absorbing device 210 A and a second absorbing device 210 B.
  • the first absorbing device 210 A and the second absorbing device 210 B both contain the moisture-absorbing polymer particles and process the humid gas stream inlet and generate the exhaust gas stream in turn;
  • a first control device 220 A to lead the humid gas stream inlet into the first absorbing device 210 A, detect the temperature of the humid gas stream inlet at the first inlet of the first absorbing device 210 A and generate a first signal of temperature, and detect the dew point of the humid gas stream inlet at the first inlet of the first absorbing device 210 A and generate a first signal of dew point;
  • a second control device 230 A to lead the exhaust gas stream generated in the first absorbing device 210 A out of the first absorbing device 210 A, detect the temperature of the exhaust gas stream at the first outlet of the first absorbing device 210 A and generate a second signal of temperature, and detect the dew point of the exhaust gas stream at the first outlet of
  • the first central processing device 240 when the ratio of the first exhaust humidity to the first feed humidity reaches a certain set point, the first central processing device 240 generates a switching signal to disable the first control device 220 A and the second control device 230 A, and enable the third control device 220 B and the fourth control device 230 B, through which to enable the dehumidifying process performed by the second absorbing device 210 B and disable the dehumidifying process performed by the first absorbing device 210 A.
  • the first central processing device 240 when the ratio of the second exhaust humidity to the second feed humidity reaches a certain set point, the first central processing device 240 generates a switching signal to disable the third control device 220 B and the fourth control device 230 B, and enable the first control device 220 A and the second control device 230 A, through which to enable the dehumidifying process performed by the first absorbing device 210 A and disable the dehumidifying process performed by the second absorbing device 210 B.
  • the second module 220 B further comprises a second central processing device 280 to detect the temperature of a regeneration feed gas and generate an instant control signal; a heating device 270 to receive the control signal and adjust the temperature of the regeneration feed gas to a regeneration temperature, the regeneration feed gas absorbs the moisture contained in the used moisture-absorbing polymer particles in the first absorbing device 210 A or the second absorbing device 210 B and forms a regeneration exhaust gas, whereupon the first module 200 A can proceed next dehumidifying process utilizing the regenerated moisture-absorbing polymer particles; a fifth control device 250 A to lead the regeneration feed gas into the first absorbing device 210 A, detect the temperature of the regeneration feed gas at the second inlet of the first absorbing device 210 A and generate a fifth signal of temperature, and detect the dew point of the regeneration feed gas at the second inlet of the first absorbing device 210 A and generate a fifth signal of dew point; a sixth control device 260 A to lead the regeneration exhaust gas generated in the first absorbing device 210 A out of the first
  • the third central processing device 290 when the third exhaust humidity equals the third feed humidity, the third central processing device 290 generates a switching signal to disable the fifth control device 250 A and the sixth control device 260 A, and enable the seventh control device 250 B and the eighth control device 260 B, through which to enable the regeneration process performed by the second absorbing device 210 B and disable the regeneration process performed by the first absorbing device 210 A.
  • the third central processing device 290 when the fourth exhaust humidity equals the fourth feed humidity, the third central processing device 290 generates a switching signal to disable the seventh control device 250 B and the eighth control device 260 B, and enable the fifth control device 250 A and the sixth control device 260 A, through which to enable the regeneration process performed by the first absorbing device 210 A and disable the regeneration process performed by the second absorbing device 210 B.
  • a continuous dehumidifying system comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the first module comprises a plurality of moisture-absorbing polymer particles to process a humid gas stream inlet and generate a exhaust gas stream; and the second module processes the used moisture-absorbing polymer particles in the first module; regenerate them and prepare for next dehumidifying process going to perform.
  • the above mentioned moisture-absorbing polymer particles contain poly-N-isopropylacrylamide (PNIPAm] crosslinking copolymer which is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds.
  • the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
  • the amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %.
  • the moisture-absorbing polymer particle can have a shell which is made of a material having sulfonic acid group, such as [poly(styrene sulfonic acid), PSSA]. What should be noticed is, the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
  • the first module further comprises a first absorbing device 300 A and a second absorbing device 300 B.
  • the first absorbing device 300 A and the second absorbing device 300 B both contain moisture-absorbing polymer particles and process the humid gas stream inlet and generate the exhaust gas stream in turn; a plurality of moisture-absorbing polymer particles 305 A in the first absorbing device 300 A and a plurality of moisture-absorbing polymer particles 305 B in the second absorbing device 300 B were used to absorb the moisture contained in the humid gas stream inlet; two supporting devices 310 A and 310 B which are located in the bottom of the first absorbing device 300 A and the second absorbing device 300 B, respectively, each of the two supporting devices 310 A and 310 B is used for bearing a stack of the moisture-absorbing polymer particles of a certain height, and each of the two supporting devices 310 A and 310 B has a plurality of holes for ventilation; a first feed control valve 315 A to lead the humid gas stream inlet into the first absorbing device 300 A; a first exhaust control valve 320 A
  • the first module further comprises a fourth temperature detector 325 B to detect the temperature of the humid gas stream inlet at the first inlet of the second absorbing device 300 B and generate a fourth signal of temperature; a fifth temperature detector 330 B to detect the gas temperature at half the certain height of the moisture-absorbing polymer particle stack in the second absorbing device 300 B and generate a fifth signal of temperature; a sixth temperature detector 335 B to detect the temperature of the exhaust gas stream at the first outlet of the second absorbing device 300 B and generate a sixth signal of temperature; a first dew point meter 340 A to detect the dew point of the humid gas stream inlet at the first inlet of the first absorbing device 300 A and generate a first signal of dew point; a second dew point meter 345 A to detect the dew point of the exhaust gas stream at the first outlet of the first absorbing device 300 A and generate a second signal of dew point; a third dew point meter 340 B to detect the dew point of the humid gas stream inlet at the first inlet of
  • a plurality of spheres are further stacked both on top of and under the plurality of moisture-absorbing polymer particles, in order to allow an uniform contact between the gas and the polymer particles.
  • at least two porous films are placed both on top of and under the particles or spheres, through which to avoid particles or spheres blow away.
  • the first module has a defogger to remove liquid micro-drops carried by the humid gas stream inlet; and the first driving device 350 has an air pump for providing driving force for the gas flow, and a flow rate controller for controlling the gas flow rate.
  • the first central processing device 355 In operation, when the ratio of the first exhaust humidity to the first feed humidity reaches a certain set point, the first central processing device 355 generates a switching signal to disable the first feed control valve 315 A and the first exhaust control valve 320 A, and enable the second feed control valve 315 B and the second exhaust control valve 320 B, through which to enable the dehumidifying process performed by the second absorbing device 300 B and disable the dehumidifying process performed by the first absorbing device 300 A.
  • the first central processing device 355 when the ratio of the second exhaust humidity to the second feed humidity reaches a certain set point, the first central processing device 355 generates a switching signal to disable the second feed control valve 315 B and the second exhaust control valve 320 B, and enable the first feed control valve 315 A and the first exhaust control valve 320 A, through which to enable the dehumidifying process performed by the first absorbing device 300 A and disable the dehumidifying process performed by the second absorbing device 300 B.
  • the second module further comprises a second central processing device 370 to detect the temperature of a regeneration feed gas and generate an instant control signal; a heating device 365 to receive the control signal and adjust the temperature of the regeneration feed gas to a regeneration temperature, the regeneration feed gas absorbs the moisture contained in the used moisture-absorbing polymer particles in the first absorbing device 300 A or the second absorbing device 300 B and forms a regeneration exhaust gas, whereupon the first module can proceed next dehumidifying process utilizing the regenerated moisture-absorbing polymer particles; a third feed control valve 380 A to lead the regeneration feed gas into the first absorbing device 300 A; a third exhaust control valve 395 A to lead the exhaust gas stream generated in the first absorbing device 300 A out of the first absorbing device 300 A; a fourth feed control valve 380 A to lead the regeneration feed gas into the second absorbing device 300 B; a fourth exhaust control valve 395 B to lead the regeneration exhaust gas generated in the second absorbing device 300 B out of the second absorbing device 300 B; a seventh temperature detector 360 A to detect
  • the second module further comprises a fifth dew point meter 375 A to detect the dew point of the regeneration feed gas at the second inlet of the first absorbing device 300 A and generate a fifth signal of dew point; a sixth dew point meter 390 A to detect the dew point of the regeneration exhaust gas at the second outlet of the first absorbing device 300 A and generate a sixth signal of dew point; a seventh dew point meter 375 B to detect the dew point of the regeneration feed gas at the second inlet of the second absorbing device 300 B and generate a seventh signal of dew point; an eighth dew point meter 390 B to detect the dew point of the regeneration exhaust gas at the second outlet of the second absorbing device 300 B and generate an eighth signal of dew point; a second driving device 400 to provide driving force for leading the regeneration feed gas into the first absorbing device 300 A or the second absorbing device 300 B, and for leading the regeneration exhaust gas out of the first absorbing device 300 A or the second absorbing device 300 B, further, the second driving device 400 can
  • the third central processing device 410 when the third exhaust humidity equals the third feed humidity, the third central processing device 410 generates a switching signal to disable the third feed control valve 380 A and the third exhaust control valve 395 A, and enable the fourth feed control valve 380 B and the fourth exhaust control valve 395 B, through which to enable the regeneration process performed by the second absorbing device 300 B and disable the regeneration process performed by the first absorbing device 300 A.
  • the third central processing device 410 when the fourth exhaust humidity equals the fourth feed humidity, the third central processing device 410 generates a switching signal to disable the fourth feed control valve 380 B and the fourth exhaust control valve 395 B, and enable the third feed control valve 380 A and the third exhaust control valve 395 A, through which to enable the regeneration process performed by the first absorbing device 300 A and disable the regeneration process performed by the second absorbing device 300 B.
  • the present invention employs the thermo-sensitive properties of PNIPAm for moisture-adsorbing/dehumidifying usage.
  • LCST lower critical solution temperature
  • the PNIPAm copolymer particles are hydrophilic and have a capacity to be swollen several times larger than its original volume.
  • the polymer chains contract and the PNIPAm copolymer particles become hydrophobic and can be rapidly dewatered.
  • the present invention is characterized by the above-mentioned low-regeneration temperature feature and through which the present invention provides a moisture-absorbing polymer particle which can serve as an energy saving dehumidifier at normal room temperature. Therefore, this present invention does have the economic advantages for industrial applications.
  • the present invention discloses a moisture-absorbing polymer particle, which either comprises PNIPAm crosslinking copolymer or a structure having PNIPAm crosslinking copolymer as a core and polymer with sulfonic acid group as a shell.
  • the present invention also discloses a method for producing the provided moisture-absorbing polymer particle and an application thereof; the application is referred to as a continuous dehumidifying system which comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Drying Of Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The present invention discloses a moisture-absorbing polymer particle, which either comprises PNIPAm crosslinking copolymer or a structure having PNIPAm crosslinking copolymer as a core and polymer with sulfonic acid group as a shell. The present invention also discloses a method for producing the provided moisture-absorbing polymer particle and an application thereof; the application is referred to as a continuous dehumidifying system which comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.

Description

    BACKGROUND OF THE INVENTION
  • 1. Field of the Invention
  • The present invention is generally related to a polymer particle, and more particularly to a moisture-absorbing polymer particle, a method for forming the same, and applications thereof.
  • 2. Description of the Prior Art
  • In the area with a high relative humidity, product quality in manufacturing industries usually suffers damages by high humidility condition. Thus, for most advanced technology industries, such as semi-conductor, optoelectronics and pharmacy, a dry manufacturing condition, to prevent quality loss usually accounts for a great proportion in the cost/profit management.
  • Conventional solid absorbents used for a dehumidifying system are molecule sieves or silica gels; however, due to their high regeneration temperatures, regeneration of these two materials requires great power consumption and a considerable consequential increase in the operation costs. In addition, as environmental issues have become highly regarded nowadays, new materials and methods to improve dehumidifying efficiency as a whole, using the least power consumption, is no doubt the trend for the following century.
    • SUMMARY OF THE INVENTION
  • In accordance with the present invention, a new moisture-absorbing polymer particle is provided. This particle can meet the requirement of low energy consumption and high dehumidifying efficiency.
  • One object of the present invention is to employ the thermo-sensitive properties of PNIPAm for moisture-adsorbing/dehumidifying usage. When at a temperature lower than its LCST (lower critical solution temperature), the PNIPAm copolymer particles are hydrophilic and have a capacity to be swollen several times larger than its original volume. When at a temperature higher than its LCST, the polymer chains contract and the PNIPAm copolymer particles become hydrophobic and can be rapidly dewatered. The present invention is characterized by the above-mentioned low-regeneration temperature feature and through which the present invention provides a moisture-absorbing polymer particle which can serve as an energy saving dehumidifier at normal room temperature. Therefore, this present invention does have the economic advantages for industrial applications.
  • Accordingly, the present invention discloses a moisture-absorbing polymer particle, which either comprises PNIPAm crosslinking copolymer or a structure having PNIPAm crosslinking copolymer as a core and polymer with sulfonic acid group as a shell. The present invention also discloses a method for producing the provided moisture-absorbing polymer particle and an application thereof; the application is referred to as a continuous dehumidifying system which comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
    • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 is a flow chart of a method for forming a moisture-absorbing polymer particle in accordance with a third embodiment of the present invention;
  • FIG. 2 is a schematic diagram illustrating a continuous dehumidifying system in accordance with a fourth embodiment of the present invention; and
  • FIG. 3 is a schematic diagram illustrating a continuous dehumidifying system in accordance with a fifth embodiment of the present invention.
    • DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • What is probed into the invention is moisture-absorbing polymer particle, method for forming the same and application thereof. Detailed descriptions of the production, structure and elements will be provided in the following in order to make the invention thoroughly understood. Obviously, the application of the invention is not confined to specific details familiar to those who are skilled in the moisture-absorbing polymer particle. On the other hand, the common elements and procedures that are known to everyone are not described in details to avoid unnecessary limits of the invention. Some preferred embodiments of the present invention will now be described in greater detail in the following. However, it should be recognized that the present invention can be practiced in a wide range of other embodiments besides those explicitly described, that is, this invention can also be applied extensively to other embodiments, and the scope of the present invention is expressly not limited except as specified in the accompanying claims.
  • In a first embodiment of the present invention, there is provided a moisture-absorbing polymer particle which comprises poly-N-isopropylacrylamide (PNIPAm] crosslinking colymer. The crosslinking copolymer is polymerized by N-isopropylacrylamide (NIPAm), as a monomer, with an acrylamide-type crosslinker having at least two double bonds, wherein the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide. The amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %.
  • In a second embodiment of the present invention, there is provided a moisture-absorbing polymer particle with a structure of a core, mainly PNIPAm, and a shell comprising polymer with sulfonic acid group. The core comprises PNIPAm crosslinking copolymer and is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds, wherein the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide. The amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %. Further, the polymer of the shell further comprises [poly(styrene sulfonic acid) PSSA].
  • Referring to FIG. 1, in a third embodiment of the present invention, a method for forming moisture-absorbing polymer particles is provided. First of all, a first mixing process 110 is performed to mix NIPAm an acrylamide-type crosslinker having at least two double bonds and water into a first solution 115, wherein the acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide. The amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %. Next, a dissolving process 120 is performed to dissolve a water-soluble initiator containing ammounium persulfate(APS) into water to form a second solution 125. The amount of the water-soluble initiator to use is selected0.5 wt %-2 wt % of NIPAm. Then, a second mixing process 130 is performed at a specific temperature to mix the first solution 115 with the second solution 125 to form a third solution 135, wherein the specific temperature is lower than 33° C. Next, a dispersion process 140 is performed at the specific temperature to uniformly distribute a plurality of liquid drops containing the third solution 135 in an organic solvent containing toluene, so as to form a water-in-oil system. Afterwards, a catalyst containing N,N,N′,N′,-Tetramethylethylendiamine (TEMED) is added into the organic solvent for starting and accelerating a polymerization 150 in the liquid drops, wherein the NIPAm and the acrylamide-type crosslinker are polymerized into a first moisture-absorbing polymer particle 155A. In detail, the first moisture-absorbing particle 155A is formed under a condition with inert gas purged, and the polymerization time is longer than 4 hours.
  • Referring to FIG. 1, in this embodiment, the provided method for forming moisture-absorbing polymer particles can further comprise at least one purification process 160 and a shell-forming process 170. The purification process 160 further comprises removing unreacted NIPAm, unreacted acrylamide-type crosslinker and impurities by an extracting agent (such as ketone), and removing the extracting agent by a cleaning agent (such as water). On the other hand, the shell-forming process 170 forms a shell region having sulfonic acid group onto the surface of the previous purifed first moisture-absorbing polymer particle 155A, and through which to form a second moisture-absorbing polymer particle 155B. The shell-forming process 170 comprises: coating a 30 wt % [poly(styrene sulfonic acid), PSSA] solution onto the surface of the previous purifed first moisture-absorbing polymer particle 155A; and performing a drying procedure to form a shell region having PSSA on the previous purifed first moisture-absorbing polymer particle 155A.
  • Referring to FIG. 2, in a fourth embodiment of the present invention, a continuous dehumidifying system is provided. The provided continuous dehumidifying system comprises a first module 200A to perform a dehumidifying process and a second module 200B to perform a regeneration process, wherein the first module comprises a plurality of moisture-absorbing polymer particles to process a humid gas stream inlet and generate a dryed exhaust stream outlet; and the second module 200B processes the used moisture-absorbing polymer particles in the first module 200A; regenates them and prepares for next dehumidifying process going to perform. The above mentioned moisture-absorbing polymer particles comprises poly-N-isopropylacrylamide (PNIPAm] crosslinking copolymer which is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds. The acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide. The amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %. Alternatively, the moisture-absorbing polymer particle can have a shell which is made of a material having sulfonic acid group, such as [poly(styrene sulfonic acid), PSSA]. The dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
  • In this embodiment, the first module 200A further comprises a first absorbing device 210A and a second absorbing device 210B. The first absorbing device 210A and the second absorbing device 210B both contain the moisture-absorbing polymer particles and process the humid gas stream inlet and generate the exhaust gas stream in turn; a first control device 220A to lead the humid gas stream inlet into the first absorbing device 210A, detect the temperature of the humid gas stream inlet at the first inlet of the first absorbing device 210A and generate a first signal of temperature, and detect the dew point of the humid gas stream inlet at the first inlet of the first absorbing device 210A and generate a first signal of dew point; a second control device 230A to lead the exhaust gas stream generated in the first absorbing device 210A out of the first absorbing device 210A, detect the temperature of the exhaust gas stream at the first outlet of the first absorbing device 210A and generate a second signal of temperature, and detect the dew point of the exhaust gas stream at the first outlet of the first absorbing device 210A and generate a second signal of dew point; a third control device 220B to lead the humid gas stream inlet into the second absorbing device 210B, detect the temperature of the humid gas stream inlet at the first inlet of the second absorbing device 210B and generate a third signal of temperature, and detect the dew point of the humid gas stream inlet at the first inlet of the second absorbing device 210B and generate a third signal of dew point; a fourth control device 230B to lead the exhaust gas stream generated in the second absorbing device 210B out of the second absorbing device 210B, detect the temperature of the exhaust gas stream at the first outlet of the second absorbing device 210B and generate a fourth signal of temperature, and detect the dew point of the exhaust gas stream at the first outlet of the second absorbing device 210B and generate a fourth signal of dew point; a first driving device 245 to provide driving force for leading the humid gas stream inlet into the first absorbing device 210A or the second absorbing device 210B, and for leading the exhaust gas stream out of the first absorbing device 210A or the second absorbing device 210B, further, the first driving device 245 can adjust the gas flow rate and according to which generate a first signal of flow rate; and a first central processing device 240 to receive the first signal of temperature, the second signal of temperature, the first signal of dew point, the second signal of dew point, and the first signal of flow rate to determine a first feed humidity describing the humid gas stream inlet at the first inlet of the first absorbing device 210A and a first exhaust humidity describing the exhaust gas stream at the first outlet of the first absorbing device 210A, on the other hand, the first central processing device 240 receives the third signal of temperature, the fourth signal of temperature, the third signal of dew point and the fourth signal of dew point, and combine with the first signal of flow rate, to determine a second feed humidity describing the humid gas stream inlet at the first inlet of the second absorbing device 210B and a second exhaust humidity describing the exhaust gas stream at the first outlet of the second absorbing device 210B.
  • In this embodiment, when the ratio of the first exhaust humidity to the first feed humidity reaches a certain set point, the first central processing device 240 generates a switching signal to disable the first control device 220A and the second control device 230A, and enable the third control device 220B and the fourth control device 230B, through which to enable the dehumidifying process performed by the second absorbing device 210B and disable the dehumidifying process performed by the first absorbing device 210A. On the other hand, when the ratio of the second exhaust humidity to the second feed humidity reaches a certain set point, the first central processing device 240 generates a switching signal to disable the third control device 220B and the fourth control device 230B, and enable the first control device 220A and the second control device 230A, through which to enable the dehumidifying process performed by the first absorbing device 210A and disable the dehumidifying process performed by the second absorbing device 210B.
  • In this embodiment, the second module 220B further comprises a second central processing device 280 to detect the temperature of a regeneration feed gas and generate an instant control signal; a heating device 270 to receive the control signal and adjust the temperature of the regeneration feed gas to a regeneration temperature, the regeneration feed gas absorbs the moisture contained in the used moisture-absorbing polymer particles in the first absorbing device 210A or the second absorbing device 210B and forms a regeneration exhaust gas, whereupon the first module 200A can proceed next dehumidifying process utilizing the regenerated moisture-absorbing polymer particles; a fifth control device 250A to lead the regeneration feed gas into the first absorbing device 210A, detect the temperature of the regeneration feed gas at the second inlet of the first absorbing device 210A and generate a fifth signal of temperature, and detect the dew point of the regeneration feed gas at the second inlet of the first absorbing device 210A and generate a fifth signal of dew point; a sixth control device 260A to lead the regeneration exhaust gas generated in the first absorbing device 210A out of the first absorbing device 210A, detect the temperature of the regeneration exhaust gas at the second outlet of the first absorbing device 210A and generate a sixth signal of temperature, and detect the dew point of the regeneration exhaust gas at the second outlet of the first absorbing device 210A and generate a sixth signal of dew point; a seventh control device 250B to lead the regeneration feed gas into the second absorbing device 210B, detect the temperature of the regeneration feed gas at the second inlet of the second absorbing device 210B and generate a seventh signal of temperature, and detect the dew point of the regeneration feed gas at the second inlet of the second absorbing device 210B and generate a seventh signal of dew point; an eighth control device 260B to lead the regeneration exhaust gas generated in the second absorbing device 210B out of the second absorbing device 210B, detect the temperature of the regeneration exhaust gas at the second outlet of the second absorbing device 210B and generate an eighth signal of temperature, and detect the dew point of the regeneration exhaust gas at the second outlet of the second absorbing device 210B and generate an eighth signal of dew point; a second driving device 285 to provide driving force for leading the regeneration feed gas into the first absorbing device 210A or the second absorbing device 210B, and for leading the regeneration exhaust gas out of the first absorbing device 210A or the second absorbing device 210B, further, the second driving device 285 can adjust the gas flow rate and according to which generate a second signal of flow rate; and a third central processing device 290 to receive the fifth signal of temperature, the sixth signal of temperature, the fifth signal of dew point, the sixth signal of dew point, and the second signal of flow rate to determine a third feed humidity describing the regeneration feed gas at the second inlet of the first absorbing device 210A and a third exhaust humidity describing the regeneration exhaust gas at the second outlet of the first absorbing device 210A, on the other hand, the third central processing device 290 receives the seventh signal of temperature, the eighth signal of temperature, the seventh signal of dew point and the eighth signal of dew point, and combine with the second signal of flow rate, to determine a fourth feed humidity describing the regeneration feed gas at the second inlet of the second absorbing device 210B and a fourth exhaust humidity describing the regeneration exhaust gas at the second outlet of the second absorbing device 210B.
  • In this embodiment, when the third exhaust humidity equals the third feed humidity, the third central processing device 290 generates a switching signal to disable the fifth control device 250A and the sixth control device 260A, and enable the seventh control device 250B and the eighth control device 260B, through which to enable the regeneration process performed by the second absorbing device 210B and disable the regeneration process performed by the first absorbing device 210A. On the other hand, when the fourth exhaust humidity equals the fourth feed humidity, the third central processing device 290 generates a switching signal to disable the seventh control device 250B and the eighth control device 260B, and enable the fifth control device 250A and the sixth control device 260A, through which to enable the regeneration process performed by the first absorbing device 210A and disable the regeneration process performed by the second absorbing device 210B.
  • In a fifth embodiment of the present invention, a continuous dehumidifying system is provided. The provided continuous dehumidifying system comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the first module comprises a plurality of moisture-absorbing polymer particles to process a humid gas stream inlet and generate a exhaust gas stream; and the second module processes the used moisture-absorbing polymer particles in the first module; regenerate them and prepare for next dehumidifying process going to perform. The above mentioned moisture-absorbing polymer particles contain poly-N-isopropylacrylamide (PNIPAm] crosslinking copolymer which is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds. The acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide. The amount of the acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm with a preferred value of 2 wt %. Alternatively, the moisture-absorbing polymer particle can have a shell which is made of a material having sulfonic acid group, such as [poly(styrene sulfonic acid), PSSA]. What should be noticed is, the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
  • In this embodiment, the first module further comprises a first absorbing device 300A and a second absorbing device 300B. The first absorbing device 300A and the second absorbing device 300B both contain moisture-absorbing polymer particles and process the humid gas stream inlet and generate the exhaust gas stream in turn; a plurality of moisture-absorbing polymer particles 305A in the first absorbing device 300A and a plurality of moisture-absorbing polymer particles 305B in the second absorbing device 300B were used to absorb the moisture contained in the humid gas stream inlet; two supporting devices 310A and 310B which are located in the bottom of the first absorbing device 300A and the second absorbing device 300B, respectively, each of the two supporting devices 310A and 310B is used for bearing a stack of the moisture-absorbing polymer particles of a certain height, and each of the two supporting devices 310A and 310B has a plurality of holes for ventilation; a first feed control valve 315A to lead the humid gas stream inlet into the first absorbing device 300A; a first exhaust control valve 320A to lead the exhaust gas stream out of the first absorbing device 300A; a second feed control valve 315B to lead the humid gas stream inlet into the second absorbing device 300B; a second exhaust control valve 320B to lead the exhaust gas stream out of the second absorbing device 300B; a first temperature detector 325A to detect the temperature of the humid gas stream inlet at the first inlet of the first absorbing device 300A and generate a first signal of temperature; a second temperature detector 330A to detect the gas temperature at half the certain height of the moisture-absorbing polymer particle stack in the first absorbing device 300A and generate a second signal of temperature; and a third temperature detector 335A to detect the temperature of the exhaust gas stream at the first outlet of the first absorbing device 300A and generate a third signal of temperature.
  • In this embodiment, the first module further comprises a fourth temperature detector 325B to detect the temperature of the humid gas stream inlet at the first inlet of the second absorbing device 300B and generate a fourth signal of temperature; a fifth temperature detector 330B to detect the gas temperature at half the certain height of the moisture-absorbing polymer particle stack in the second absorbing device 300B and generate a fifth signal of temperature; a sixth temperature detector 335B to detect the temperature of the exhaust gas stream at the first outlet of the second absorbing device 300B and generate a sixth signal of temperature; a first dew point meter 340A to detect the dew point of the humid gas stream inlet at the first inlet of the first absorbing device 300A and generate a first signal of dew point; a second dew point meter 345A to detect the dew point of the exhaust gas stream at the first outlet of the first absorbing device 300A and generate a second signal of dew point; a third dew point meter 340B to detect the dew point of the humid gas stream inlet at the first inlet of the second absorbing device 300B and generate a third signal of dew point; a fourth dew point meter 345B to detect the dew point of the exhaust gas stream at the first outlet of the second absorbing device 300B and generate a fourth signal of dew point; a first driving device 350 to provide driving force for leading the humid gas stream inlet into the first absorbing device 300A or the second absorbing device 300B, and for leading the exhaust gas stream out of the first absorbing device 300A or the second absorbing device 300B, further, the first driving device 350 can adjust the gas flow rate and according to which generate a first signal of flow rate; and a first central processing device 355 to receive the first signal of temperature, the second signal of temperature, the third signal of temperature, the first signal of dew point, the second signal of dew point, and the first signal of flow rate to determine a first feed humidity describing the humid gas stream inlet at the first inlet of the first absorbing device 300A and a first exhaust humidity describing the exhaust gas stream at the first outlet of the first absorbing device 300A, on the other hand, the first central processing device 355 receives the fourth signal of temperature, the fifth signal of temperature, the sixth signal of temperature, the third signal of dew point and the fourth signal of dew point, and combine with the first signal of flow rate, to determine a second feed humidity describing the humid gas stream inlet at the first inlet of the second absorbing device 300B and a second exhaust humidity describing the exhaust gas stream at the first outlet of the second absorbing device 300B.
  • In this embodiment, a plurality of spheres are further stacked both on top of and under the plurality of moisture-absorbing polymer particles, in order to allow an uniform contact between the gas and the polymer particles. Additionally, at least two porous films are placed both on top of and under the particles or spheres, through which to avoid particles or spheres blow away. Moreover, the first module has a defogger to remove liquid micro-drops carried by the humid gas stream inlet; and the first driving device 350 has an air pump for providing driving force for the gas flow, and a flow rate controller for controlling the gas flow rate. In operation, when the ratio of the first exhaust humidity to the first feed humidity reaches a certain set point, the first central processing device 355 generates a switching signal to disable the first feed control valve 315A and the first exhaust control valve 320A, and enable the second feed control valve 315B and the second exhaust control valve 320B, through which to enable the dehumidifying process performed by the second absorbing device 300B and disable the dehumidifying process performed by the first absorbing device 300A. On the other hand, when the ratio of the second exhaust humidity to the second feed humidity reaches a certain set point, the first central processing device 355 generates a switching signal to disable the second feed control valve 315B and the second exhaust control valve 320B, and enable the first feed control valve 315A and the first exhaust control valve 320A, through which to enable the dehumidifying process performed by the first absorbing device 300A and disable the dehumidifying process performed by the second absorbing device 300B.
  • In this embodiment, the second module further comprises a second central processing device 370 to detect the temperature of a regeneration feed gas and generate an instant control signal; a heating device 365 to receive the control signal and adjust the temperature of the regeneration feed gas to a regeneration temperature, the regeneration feed gas absorbs the moisture contained in the used moisture-absorbing polymer particles in the first absorbing device 300A or the second absorbing device 300B and forms a regeneration exhaust gas, whereupon the first module can proceed next dehumidifying process utilizing the regenerated moisture-absorbing polymer particles; a third feed control valve 380A to lead the regeneration feed gas into the first absorbing device 300A; a third exhaust control valve 395A to lead the exhaust gas stream generated in the first absorbing device 300A out of the first absorbing device 300A; a fourth feed control valve 380A to lead the regeneration feed gas into the second absorbing device 300B; a fourth exhaust control valve 395B to lead the regeneration exhaust gas generated in the second absorbing device 300B out of the second absorbing device 300B; a seventh temperature detector 360A to detect the temperature of the regeneration feed gas at the second inlet of the first absorbing device 300A and generate a seventh signal of temperature; an eighth temperature detector 385A to detect the temperature of the regeneration exhaust gas at the second outlet of the first absorbing device 300A and generate an eighth signal of temperature; a ninth temperature detector 360B to detect the temperature of the regeneration feed gas at the second inlet of the second absorbing device 300B and generate a ninth signal of temperature; and a tenth temperature detector 385B to detect the temperature of the regeneration exhaust gas at the second outlet of the second absorbing device 300B and generate a tenth signal of temperature.
  • In this embodiment, the second module further comprises a fifth dew point meter 375A to detect the dew point of the regeneration feed gas at the second inlet of the first absorbing device 300A and generate a fifth signal of dew point; a sixth dew point meter 390A to detect the dew point of the regeneration exhaust gas at the second outlet of the first absorbing device 300A and generate a sixth signal of dew point; a seventh dew point meter 375B to detect the dew point of the regeneration feed gas at the second inlet of the second absorbing device 300B and generate a seventh signal of dew point; an eighth dew point meter 390B to detect the dew point of the regeneration exhaust gas at the second outlet of the second absorbing device 300B and generate an eighth signal of dew point; a second driving device 400 to provide driving force for leading the regeneration feed gas into the first absorbing device 300A or the second absorbing device 300B, and for leading the regeneration exhaust gas out of the first absorbing device 300A or the second absorbing device 300B, further, the second driving device 400 can adjust the gas flow rate and according to which generate a second signal of flow rate; and a third central processing device 410 to receive the seventh signal of temperature, the eighth signal of temperature, the fifth signal of dew point, the sixth signal of dew point, and the second signal of flow rate to determine a third feed humidity describing the regeneration feed gas at the second inlet of the first absorbing device 300A and a third exhaust humidity describing the regeneration exhaust gas at the second outlet of the first absorbing device 300A, on the other hand, the third central processing device 410 receives the ninth signal of temperature, the tenth signal of temperature, the seventh signal of dew point and the eighth signal of dew point, and combine with the second signal of flow rate, to determine a fourth feed humidity describing the regeneration feed gas at the second inlet of the second absorbing device 300B and a fourth exhaust humidity describing the regeneration exhaust gas at the second outlet of the second absorbing device 300B.
  • In this embodiment, when the third exhaust humidity equals the third feed humidity, the third central processing device 410 generates a switching signal to disable the third feed control valve 380A and the third exhaust control valve 395A, and enable the fourth feed control valve 380B and the fourth exhaust control valve 395B, through which to enable the regeneration process performed by the second absorbing device 300B and disable the regeneration process performed by the first absorbing device 300A. On the other hand, when the fourth exhaust humidity equals the fourth feed humidity, the third central processing device 410 generates a switching signal to disable the fourth feed control valve 380B and the fourth exhaust control valve 395B, and enable the third feed control valve 380A and the third exhaust control valve 395A, through which to enable the regeneration process performed by the first absorbing device 300A and disable the regeneration process performed by the second absorbing device 300B.
  • In the above preferred embodiments, the present invention employs the thermo-sensitive properties of PNIPAm for moisture-adsorbing/dehumidifying usage. When at a temperature lower than its LCST (lower critical solution temperature), the PNIPAm copolymer particles are hydrophilic and have a capacity to be swollen several times larger than its original volume. When at a temperature higher than its LCST, the polymer chains contract and the PNIPAm copolymer particles become hydrophobic and can be rapidly dewatered. The present invention is characterized by the above-mentioned low-regeneration temperature feature and through which the present invention provides a moisture-absorbing polymer particle which can serve as an energy saving dehumidifier at normal room temperature. Therefore, this present invention does have the economic advantages for industrial applications.
  • To sum up, the present invention discloses a moisture-absorbing polymer particle, which either comprises PNIPAm crosslinking copolymer or a structure having PNIPAm crosslinking copolymer as a core and polymer with sulfonic acid group as a shell. The present invention also discloses a method for producing the provided moisture-absorbing polymer particle and an application thereof; the application is referred to as a continuous dehumidifying system which comprises a first module to perform a dehumidifying process and a second module to perform a regeneration process, wherein the dehumidifying process is performed at a temperature lower than 33° C. and the regeneration process is performed at a temperature higher than 40° C.
  • Obviously many modifications and variations are possible in light of the above teachings. It is therefore to be understood that within the scope of the appended claims the present invention can be practiced otherwise than as specifically described herein. Although specific embodiments have been illustrated and described herein, it is obvious to those skilled in the art that many modifications of the present invention may be made without departing from what is intended to be limited solely by the appended claims.

Claims (61)

1. A moisture-absorbing polymer particle which comprises poly-N-isopropylacrylamide (PNIPAm] crosslinking copolymer.
2. The moisture-absorbing polymer particle in claim 1, wherein said crosslinking copolymer is polymerized by N-isopropylacrylamide (NIPAm), as a monomer, with an acrylamide-type crosslinker having at least two double bonds.
3. The moisture-absorbing polymer particle in claim 2, wherein said acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
4. The moisture-absorbing polymer particle in claim 2, wherein the amount of said acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm.
5. The moisture-absorbing polymer particle in claim 2, wherein the preferred amount of said acrylamide-type crosslinker added is 2 wt % of NIPAm.
6. A moisture-absorbing polymer particle with a structure of:
a core comprising PNIPAm crosslinking copolymer; and
a shell comprising polymer with sulfonic acid group.
7. The moisture-absorbing polymer particle in claim 6, wherein said PNIPAm crosslinking copolymer is polymerzed by NIPAm with an acrylamide-type crosslinker having at least two double bonds.
8. The moisture-absorbing polymer particle in claim 7, wherein said acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
9. The moisture-absorbing polymer particle in claim 7, wherein the amount of said acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm.
10. The moisture-absorbing polymer particle in claim 7, wherein the preferred amount of said acrylamide-type crosslinker added is 2 wt % of NIPAm.
11. The moisture-absorbing polymer particle in claim 6, wherein the polymer of said shell further comprises [poly(styrene sulfonic acid), PSSA].
12. A method for forming a moisture-absorbing polymer particle, comprising:
mixing NIPAm, as a monomer, a acrylamide-type crosslinker having at least two double bonds, and water to form a first solution;
dissolving a water-soluble initiator into water to form a second solution;
mixing said first solution with said second solution at a specific temperature to form a third solution;
performing a dispersion process at said specific temperature to distribute a plurality of liquid drops containing said third solution in an organic solvent; and
adding a catalyst into said organic solvent at said specific temperature for starting and accelerating a polymerization in said plurality of liquid drops, wherein NIPAm, as a monomer, and said acrylamide-type crosslinker are polymerized into a first moisture-absorbing polymer particle.
13. The method in claim 12, wherein said acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
14. The method in claim 12, wherein the amount of said acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm.
15. The method in claim 12, wherein the preferred amount of said acrylamide-type crosslinker added is 2 wt % of NIPAm.
16. The method in claim 12, wherein said water-soluble initiator comprises ammounium persulfate(APS).
17. The method in claim 12, wherein the amount of said water-soluble initiator is selected 0.5 wt %-2 wt % of NIPAm.
18. The method in claim 12, wherein said specific temperature is lower than 33° C.
19. The method in claim 12, wherein said organic solvent comprises toluene.
20. The method in claim 12, wherein said catalyst comprises N,N,N′,N′,-Tetramethylethylendiamine (TEMED).
21. The method in claim 12, wherein said polymerization time is longer than 4 hours.
22. The method in claim 12, wherein said first moisture-absorbing particle is formed under a condition with inert gas purged.
23. The method in claim 12, further comprising:
performing at least one purification process to remove unreacted NIPAm, unreacted acrylamide-type crosslinker and impurities; and
performing a shell-forming process to form a shell region having sulfonic acid group onto the surface of the previous purifed first moisture-absorbing polymer particle, and through which to form a second moisture-absorbing polymer particle.
24. The method in claim 23, wherein at least one said purification process further comprises:
removing unreacted NIPAm, unreacted acrylamide-type crosslinker and impurities by an extracting agent; and
removing said extracting agent by a cleaning agent.
25. The method in claim 24, wherein said extracting agent comprises ketone.
26. The method in claim 24, wherein said cleaning agent comprises water.
27. The method in claim 23, wherein said shell-forming process further comprises:
coating a [poly(styrene sulfonic acid), PSSA] solution onto the surface of the previous purifed first moisture-absorbing polymer particle; and
performing a drying procedure to form a shell region having PSSA on the previous purifed first moisture-absorbing polymer particle.
28. The method in claim 27, wherein said PSSA solution comprises 30 wt % PSSA.
29. a continuous dehumidifying system, comprising:
a first module to perform a dehumidifying process, said first module comprises a plurality of moisture-absorbing polymer particles to process a humid gas stream inlet and generate a dryed exhaust stream outlet; and
a second module to perform a regeneration process, said second module processes used said plurality of moisture-absorbing polymer particles in said first module; regenerate them and prepare for next dehumidifying process going to perform, said plurality of moisture-absorbing polymer particles further comprises poly-N-isopropylacrylamide (PNIPAm] crosslinking copolymer.
30. The continuous dehumidifying system in claim 29, wherein said dehumidifying process is performed at a temperature lower than 33° C.
31. The continuous dehumidifying system in claim 29, wherein said regeneration process is performed at a temperature higher than 40° C.
32. The continuous dehumidifying system in claim 29, wherein said first module further comprises:
a first absorbing device and a second absorbing device, said first absorbing device and said second absorbing device both contain said plurality of moisture-absorbing polymer particles and process said humid gas stream inlet and generate said exhaust gas stream in turn;
a first control device to lead said humid gas stream inlet into said first absorbing device, detect the temperature of the humid gas stream inlet at a first inlet of the first absorbing device and generate a first signal of temperature, and detect the dew point of said humid gas stream inlet at said first inlet of said first absorbing device and generate a first signal of dew point;
a second control device to lead said exhaust gas stream generated in said first absorbing device out of said first absorbing device, detect the temperature of said exhaust gas stream at a first outlet of said first absorbing device and generate a second signal of temperature, and detect the dew point of said exhaust gas stream at said first outlet of said first absorbing device and generate a second signal of dew point;
a third control device to lead said humid gas stream inlet into said second absorbing device, detect the temperature of said humid gas stream inlet at a first inlet of said second absorbing device and generate a third signal of temperature, and detect the dew point of said humid gas stream inlet at said first inlet of said second absorbing device and generate a third signal of dew point;
a fourth control device to lead said exhaust gas stream generated in said first absorbing device out of said second absorbing device, detect the temperature of said exhaust gas stream at a first inlet of said second absorbing device and generate a fourth signal of temperature, and detect the dew point of said exhaust gas stream at said first outlet of said second absorbing device and generate a fourth signal of dew point;
a first driving device to provide driving force for leading the humid gas stream inlet into said first absorbing device or said second absorbing device, and for leading said exhaust gas stream out of said first absorbing device or said second absorbing device, further, said first driving device can adjust the gas flow rate and according to which generate a first signal of flow rate; and
a first central processing device to receive said first signal of temperature, said second signal of temperature, said first signal of dew point, said second signal of dew point, and said first signal of flow rate to determine a first feed humidity describing said humid gas stream inlet at said first inlet of the first absorbing device and a first exhaust humidity describing said exhaust gas stream at said first outlet of said first absorbing device, on the other hand, said first central processing device receives said third signal of temperature, said fourth signal of temperature, said third signal of dew point and said fourth signal of dew point, and combine with said first signal of flow rate, to determine a second feed humidity describing said humid gas stream inlet at said first inlet of said second absorbing device and a second exhaust humidity describing said exhaust gas stream at said first outlet of said second absorbing device.
33. The continuous dehumidifying system in claim 32, wherein when the ratio of said first exhaust humidity to said first feed humidity reaches a certain set point, said first central processing device generates a switching signal to disable said first control device and said second control device, and enable said third control device and said fourth control device, through which to enable said dehumidifying process performed by said second absorbing device and disable said dehumidifying process performed by said first absorbing device.
34. The continuous dehumidifying system in claim 32, wherein when the ratio of said second exhaust humidity to said second feed humidity reaches a certain set point, said first central processing device generates a switching signal to disable said third control device and said fourth control device, and enable said first control device and said second control device, through which to enable said dehumidifying process performed by said first absorbing device and disable said dehumidifying process performed by said second absorbing device.
35. The continuous dehumidifying system in claim 29, wherein said second module further comprises:
a second central processing device to detect the temperature of a regeneration feed gas and generate an instant control signal;
a heating device to receive said control signal and adjust the temperature of said regeneration feed gas to a regeneration temperature, said regeneration feed gas absorbs the moisture contained in used said plurality of moisture-absorbing polymer particles in said first absorbing device or said second absorbing device and forms a regeneration exhaust gas, whereupon said first module can proceed next dehumidifying process utilizing regenerated said moisture-absorbing polymer particles;
a fifth control device to lead said regeneration feed gas into said first absorbing device, detect the temperature of said regeneration feed gas at a second inlet of said first absorbing device and generate a fifth signal of temperature, and detect the dew point of said regeneration feed gas at said second inlet of said first absorbing device and generate a fifth signal of dew point;
a sixth control device to lead said regeneration exhaust gas generated in said first absorbing device out of said first absorbing device, detect the temperature of said regeneration exhaust gas at a second outlet of said first absorbing device and generate a sixth signal of temperature, and detect the dew point of said regeneration exhaust gas at said second outlet of said first absorbing device and generate a sixth signal of dew point;
a seventh control device to lead said regeneration feed gas into said second absorbing device, detect the temperature of said regeneration feed gas at a second inlet of said second absorbing device and generate a seventh signal of temperature, and detect the dew point of said regeneration feed gas at said second inlet of said second absorbing device and generate a seventh signal of dew point;
an eighth control device to lead said regeneration exhaust gas generated in said second absorbing device out of said second absorbing device, detect the temperature of said regeneration exhaust gas at said second outlet of said second absorbing device and generate an eighth signal of temperature, and detect the dew point of said regeneration exhaust gas at said second outlet of said second absorbing device and generate an eighth signal of dew point;
a second driving device to provide driving force for leading said regeneration feed gas into said first absorbing device or said second absorbing device, and for leading said regeneration exhaust gas out of said first absorbing device or said second absorbing device, further, said second driving device can adjust the gas flow rate and according to which generate a second signal of flow rate; and
a third central processing device to receive said fifth signal of temperature, said sixth signal of temperature, said fifth signal of dew point, said sixth signal of dew point, and said second signal of flow rate to determine a third feed humidity describing said regeneration feed gas at said second inlet of said first absorbing device and a third exhaust humidity describing said regeneration exhaust gas at said second outlet of said first absorbing device, on the other hand, said third central processing device receives said seventh signal of temperature, said eighth signal of temperature, said seventh signal of dew point and said eighth signal of dew point, and combine with said second signal of flow rate, to determine a fourth feed humidity describing said regeneration feed gas at said second inlet of said second absorbing device and a fourth exhaust humidity describing said regeneration exhaust gas at said second outlet of said second absorbing device.
36. The continuous dehumidifying system in claim 35, wherein when said third exhaust humidity equals said third feed humidity, said third central processing device generates a switching signal to disable said fifth control device and said sixth control device, and enable said seventh control device and said eighth control device, through which to enable said regeneration process performed by said second absorbing device and disable said regeneration process performed by said first absorbing device.
37. The continuous dehumidifying system in claim 35, wherein when said fourth exhaust humidity equals said fourth feed humidity, said third central processing device generates a switching signal to disable said seventh control device and said eighth control device, and enable said fifth control device and said sixth control device, through which to enable said regeneration process performed by said first absorbing device and disable said regeneration process performed by said second absorbing device.
38. The continuous dehumidifying system in claim 29, wherein said PNIPAm crosslinking copolymer is polymerzed by NIPAm and a acrylamide-type crosslinker having at least two double bonds.
39. The continuous dehumidifying system in claim 38, wherein said acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
40. The continuous dehumidifying system in claim 38, wherein the amount of said acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm.
41. The continuous dehumidifying system in claim 38, wherein the preferred amount of said acrylamide-type crosslinker added is 2 wt % of NIPAm.
42. The continuous dehumidifying system in claim 29, wherein said moisture-absorbing polymer particle has a shell region having sulfonic acid group.
43. The continuous dehumidifying system in claim 42, wherein the material of said shell is [poly(styrene sulfonic acid), PSSA).
44. A continuous dehumidifying system, comprising:
a first module to perform a dehumidifying process, said first module comprises a plurality of moisture-absorbing polymer particles to process a humid gas stream inlet and generate a dryed exhaust stream outlet; and
a second module to perform a regeneration process, said second module processes used said plurality of moisture-absorbing polymer particles in said first module ; regenerate them and prepare for next dehumidifying process going to perform, said plurality of moisture-absorbing polymer particles further comprises poly-N-isopropylacrylamide (PNIPAml crosslinking copolymer.
45. The continuous dehumidifying system in claim 44, wherein said dehumidifying process is performed at a temperature lower than 33° C.
46. The continuous dehumidifying system in claim 44, wherein said regeneration process is performed at a temperature higher than 40° C.
47. The continuous dehumidifying system in claim 44, wherein said first module further comprises:
a first absorbing device and a second absorbing device, said first absorbing device and said second absorbing device both contain said plurality of moisture-absorbing polymer particles and process said humid gas stream inlet and generate said exhaust gas stream in turn;
said plurality of moisture-absorbing polymer particles in said first absorbing device and the second absorbing device, were used to absorb the moisture contained in said humid gas stream inlet;
two supporting devices which are located in the bottom of said first absorbing device and said second absorbing device, respectively, each of said two supporting devices is used for bearing a stack of said plurality of moisture-absorbing polymer particles of a certain height, and each of said two supporting devices has a plurality of holes for ventilation;
a first feed control valve to lead said humid gas stream inlet into said first absorbing device;
a first exhaust control valve to lead said exhaust gas stream generated in said first absorbing device out of said first absorbing device;
a second feed control valve to lead said humid gas stream inlet into said second absorbing device;
a second exhaust control valve to lead said exhaust gas stream generated in said second absorbing device out of said second absorbing device;
a first temperature detector to detect the temperature of said humid gas stream inlet at a first inlet of said first absorbing device and generate a first signal of temperature;
a second temperature detector to detect the gas temperature at half said certain height of said plurality of moisture-absorbing polymer particle stack in said first absorbing device and generate a first signal of temperature;
a third temperature detector to detect the temperature of said exhaust gas stream at a first outlet of said first absorbing device and generate a third signal of temperature;
a fourth temperature detector to detect the temperature of said humid gas stream inlet at a first inlet of said second absorbing device and generate a fourth signal of temperature;
a fifth temperature detector to detect the gas temperature at half said certain height of said plurality of moisture-absorbing polymer particle stack in said second absorbing device and generate a fifth signal of temperature;
a sixth temperature detector to detect the temperature of said exhaust gas stream at a first outlet of said second absorbing device and generate a sixth signal of temperature;
a first dew point meter to detect the dew point of said humid gas stream inlet at said first inlet of said first absorbing device and generate a first signal of dew point;
a second dew point meter to detect the dew point of said exhaust gas stream at said first outlet of said first absorbing device and generate a second signal of dew point;
a third dew point meter to detect the dew point of said humid gas stream inlet at said first inlet of said second absorbing device and generate a third signal of dew point;
a fourth dew point meter to detect the dew point of said exhaust gas stream at said first outlet of said second absorbing device and generate a fourth signal of dew point;
a first driving device to provide driving for leading said humid gas stream inlet into said first absorbing device or said second absorbing device, and for leading said exhaust gas stream out of said first absorbing device or said second absorbing device, further, said first driving device can adjust the gas flow rate and according to which generate a first signal of flow rate; and
a first central processing device to receive said first signal of temperature, said second signal of temperature, said third signal of temperature, said first signal of dew point, said second signal of dew point, and said first signal of flow rate to determine a first feed humidity describing said humid gas stream inlet at said first inlet of said first absorbing device and a first exhaust humidity describing said exhaust gas stream at said first outlet of said first absorbing device, on the other hand, said first central processing device receives said fourth signal of temperature, said fifth signal of temperature, said sixth signal of temperature, said third signal of dew point and said fourth signal of dew point, and combine with said first signal of flow rate, to determine a second feed humidity describing said humid gas stream inlet at said first inlet of said second absorbing device and a second exhaust humidity describing said exhaust gas stream at said first outlet of said second absorbing device.
48. The continuous dehumidifying system in claim 47, wherein a plurality of spheres are further stacked both on top of and under said plurality of moisture-absorbing polymer particles, in order to allow an uniform contact between the gas and the polymer particles.
49. The continuous dehumidifying system in claim 47, wherein said first module has a defogger to remove liquid micro-drops carried by said humid gas stream inlet.
50. The continuous dehumidifying system in claim 47, wherein said first driving device has an air pump for providing driving force for the gas flow, and a flow rate controller for controlling the gas flow rate.
51. The continuous dehumidifying system in claim 47, wherein when the ratio of said first exhaust humidity to said first feed humidity reaches a certain set point, said first central processing device generates a switching signal to disable said first feed control valve and said first exhaust control valve, and enable said second feed control valve and said second exhaust control valve, through which to enable said dehumidifying process performed by said second absorbing device and disable said dehumidifying process performed by said first absorbing device.
52. The continuous dehumidifying system in claim 47, wherein when the ratio of said second exhaust humidity to said second feed humidity reaches a certain set point, said first central processing device generates a switching signal to disable said second feed control valve and said second exhaust control valve, and enable said first feed control valve and said first exhaust control valve, through which to enable said dehumidifying process performed by said first absorbing device and disable said dehumidifying process performed by said second absorbing device.
53. The continuous dehumidifying system in claim 44, wherein said second module further comprises:
a second central processing device to detect the temperature of a regeneration feed gas and generate an instant control signal;
a heating device to receive said control signal and adjust the temperature of said regeneration feed gas to a regeneration temperature, said regeneration feed gas absorbs the moisture contained in used said moisture-absorbing polymer particles in said first absorbing device or said second absorbing device and forms a regeneration exhaust gas, whereupon said first module can proceed next dehumidifying process utilizing regenerated said moisture-absorbing polymer particles;
a third feed control valve to lead said regeneration feed gas into said first absorbing device;
a third exhaust control valve to lead a regeneration exhaust gas generated in said first absorbing device out of said first absorbing device;
a fourth feed control valve to lead said regeneration feed gas into said second absorbing device;
a fourth exhaust control valve to lead a regeneration exhaust gas generated in said second absorbing device out of said second absorbing device;
a seventh temperature detector to detect the temperature of said regeneration feed gas at a second inlet of said first absorbing device and generate a seventh signal of temperature;
an eighth temperature detector to detect the temperature of said regeneration exhaust gas at a second outlet of said first absorbing device and generate an eighth signal of temperature;
a ninth temperature detector to detect the temperature of said regeneration feed gas at a second inlet of said second absorbing device and generate a ninth signal of temperature;
a tenth temperature detector to detect the temperature of said regeneration exhaust gas at a second outlet of said second absorbing device and generate a tenth signal of temperature.
a fifth dew point meter to detect the dew point of said regeneration feed gas at said second inlet of said first absorbing device and generate a fifth signal of dew point;
a sixth dew point meter to detect the dew point of said regeneration exhaust gas at said second outlet of said first absorbing device and generate a sixth signal of dew point;
a seventh dew point meter to detect the dew point of said regeneration feed gas at said second inlet of said second absorbing device and generate a seventh signal of dew point;
an eighth dew point meter to detect the dew point of said regeneration exhaust gas at said second outlet of said second absorbing device and generate an eighth signal of dew point;
a second driving device to provide driving for leading said regeneration feed gas into said first absorbing device or said second absorbing device, and for leading said regeneration exhaust gas out of said first absorbing device or said second absorbing device, further, said second driving device can adjust the gas flow rate and according to which generate a second signal of flow rate; and
a third central processing device to receive said seventh signal of temperature, said eighth signal of temperature, said fifth signal of dew point, said sixth signal of dew point, and said second signal of flow rate to determine a third feed humidity describing said regeneration feed gas at said second inlet of said first absorbing device and a third exhaust humidity describing said regeneration exhaust gas at said second outlet of said first absorbing device, on the other hand, said third central processing device receives said ninth signal of temperature, said tenth signal of temperature, said seventh signal of dew point and said eighth signal of dew point, and combine with said second signal of flow rate, to determine a fourth feed humidity describing said regeneration feed gas at said second inlet of said second absorbing device and a fourth exhaust humidity describing said regeneration exhaust gas at said second outlet of said second absorbing device.
54. The continuous dehumidifying system in claim 53, wherein when said third exhaust humidity equals said third feed humidity, said third central processing device generates a switching signal to disable said third feed control valve and said third exhaust control valve, and enable said fourth feed control valve and said fourth exhaust control valve, through which to enable said regeneration process performed by said second absorbing device and disable said regeneration process performed by said first absorbing device.
55. The continuous dehumidifying system in claim 53, wherein when said fourth exhaust humidity equals said fourth feed humidity, said third central processing device generates a switching signal to disable said fourth feed control valve and said fourth exhaust control valve, and enable said third feed control valve and said third exhaust control valve, through which to enable said regeneration process performed by said first absorbing device and disable said regeneration process performed by said second absorbing device.
56. The continuous dehumidifying system in claim 44, wherein said PNIPAm crosslinking copolymer is polymerzed by NIPAm and a acrylamide-type crosslinker having at least two double bonds.
57. The continuous dehumidifying system in claim 56, wherein said acrylamide-type crosslinker is selected as anyone or any combination of the following: N,N′-diallyltartardiamide, N′-methylene-bisacrylamide(MBAAm), N,N′-hexamethylenebisacrylamide, N,N′-methylenebishydroxymethylacrylamide, and glyoxalbisacrylamide.
58. The continuous dehumidifying system in claim 56, wherein the amount of said acrylamide-type crosslinker added is selected 0.5 wt %-6 wt % of NIPAm.
59. The continuous dehumidifying system in claim 56, wherein the preferred amount of said acrylamide-type crosslinker added is 2 wt % of NIPAm.
60. The continuous dehumidifying system in claim 44, wherein said moisture-absorbing polymer particle has a shell region having sulfonic acid group.
61. The continuous dehumidifying system in claim 60, wherein the material of said shell is [poly(styrene sulfonic acid), PSSA].
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