CN112642404A - 一种可降解吸附剂及其制备方法、应用 - Google Patents
一种可降解吸附剂及其制备方法、应用 Download PDFInfo
- Publication number
- CN112642404A CN112642404A CN202011381180.4A CN202011381180A CN112642404A CN 112642404 A CN112642404 A CN 112642404A CN 202011381180 A CN202011381180 A CN 202011381180A CN 112642404 A CN112642404 A CN 112642404A
- Authority
- CN
- China
- Prior art keywords
- degradable
- adsorbent
- solution
- activated carbon
- adsorbent according
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000003463 adsorbent Substances 0.000 title claims abstract description 35
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 46
- 108010010803 Gelatin Proteins 0.000 claims abstract description 26
- 229920000159 gelatin Polymers 0.000 claims abstract description 26
- 239000008273 gelatin Substances 0.000 claims abstract description 26
- 235000019322 gelatine Nutrition 0.000 claims abstract description 26
- 235000011852 gelatine desserts Nutrition 0.000 claims abstract description 26
- 239000000243 solution Substances 0.000 claims abstract description 23
- 239000003960 organic solvent Substances 0.000 claims abstract description 9
- 238000009777 vacuum freeze-drying Methods 0.000 claims abstract description 9
- 239000003431 cross linking reagent Substances 0.000 claims abstract description 8
- 239000000839 emulsion Substances 0.000 claims abstract description 8
- 239000007864 aqueous solution Substances 0.000 claims abstract description 7
- 230000001804 emulsifying effect Effects 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract description 7
- 239000004094 surface-active agent Substances 0.000 claims abstract description 7
- 239000012535 impurity Substances 0.000 claims abstract description 5
- 238000000926 separation method Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 13
- 239000002245 particle Substances 0.000 claims description 10
- 241000609240 Ambelania acida Species 0.000 claims description 9
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- 239000010905 bagasse Substances 0.000 claims description 9
- 235000007201 Saccharum officinarum Nutrition 0.000 claims description 7
- 240000000111 Saccharum officinarum Species 0.000 claims description 7
- 238000004042 decolorization Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 6
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 claims description 6
- 229940057995 liquid paraffin Drugs 0.000 claims description 4
- -1 sorbitan fatty acid ester Chemical class 0.000 claims description 4
- XZIIFPSPUDAGJM-UHFFFAOYSA-N 6-chloro-2-n,2-n-diethylpyrimidine-2,4-diamine Chemical compound CCN(CC)C1=NC(N)=CC(Cl)=N1 XZIIFPSPUDAGJM-UHFFFAOYSA-N 0.000 claims description 3
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 3
- 229930195729 fatty acid Natural products 0.000 claims description 3
- 239000000194 fatty acid Substances 0.000 claims description 3
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 3
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 3
- 229940035044 sorbitan monolaurate Drugs 0.000 claims description 3
- 229930006000 Sucrose Natural products 0.000 abstract description 9
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 abstract description 9
- 229960004793 sucrose Drugs 0.000 abstract description 8
- 238000001179 sorption measurement Methods 0.000 abstract description 5
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000004005 microsphere Substances 0.000 description 7
- NWGKJDSIEKMTRX-AAZCQSIUSA-N Sorbitan monooleate Chemical group CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O NWGKJDSIEKMTRX-AAZCQSIUSA-N 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 235000013336 milk Nutrition 0.000 description 3
- 239000008267 milk Substances 0.000 description 3
- 210000004080 milk Anatomy 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 238000002336 sorption--desorption measurement Methods 0.000 description 2
- 239000005720 sucrose Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 229920001213 Polysorbate 20 Polymers 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- GBAOBIBJACZTNA-UHFFFAOYSA-L calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 1
- 235000010261 calcium sulphite Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 239000008395 clarifying agent Substances 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 239000000256 polyoxyethylene sorbitan monolaurate Substances 0.000 description 1
- 235000010486 polyoxyethylene sorbitan monolaurate Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- 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
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
-
- 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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
- B01J20/28021—Hollow particles, e.g. hollow spheres, microspheres or cenospheres
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/12—Purification of sugar juices using adsorption agents, e.g. active carbon
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/12—Purification of sugar juices using adsorption agents, e.g. active carbon
- C13B20/123—Inorganic agents, e.g. active carbon
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/12—Purification of sugar juices using adsorption agents, e.g. active carbon
- C13B20/126—Organic agents, e.g. polyelectrolytes
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/46—Materials comprising a mixture of inorganic and organic materials
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4806—Sorbents characterised by the starting material used for their preparation the starting material being of inorganic character
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/4856—Proteins, DNA
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Electrochemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明公开了一种可降解吸附剂的制备方法,包括如下步骤:将活性炭在明胶水溶液中分散均匀得到溶液A,将溶液A与有机溶剂、表面活性剂混匀乳化得到乳化液,然后用交联剂固化,固液分离,真空冷冻干燥得到可降解吸附剂。本发明还公开了一种可降解吸附剂,按照上述可降解吸附剂的制备方法制得。本发明还公开了上述可降解吸附剂在甘蔗糖液除杂脱色中的应用。本发明具有良好的吸附性能,可重复利用,且可以降解不会污染环境。
Description
技术领域
本发明涉及吸附剂技术领域,尤其涉及一种可降解吸附剂及其制备方法、应用。
背景技术
在蔗糖,是食糖的主要成分。广泛应用于各行各业,尤其是食品和药用辅料中。在蔗糖制备工艺中,常需要对蔗汁、糖浆等物料进行澄清处理。
目前甘蔗糖厂常采用亚硫酸法澄清生产工艺,以二氧化硫与石灰乳反应生成的亚硫酸钙为主要的澄清剂和脱色剂,所产白糖存在残硫问题,不能满足医药、食品的需求。另外,蔗糖制糖过程中,会产生大量甘蔗渣,其堆积和废弃会污染环境。
发明内容
基于背景技术存在的技术问题,本发明提出了一种可降解吸附剂及其制备方法、应用,本发明具有良好的吸附性能,可重复利用,且可以降解不会污染环境。
本发明提出的一种可降解吸附剂的制备方法,包括如下步骤:将活性炭在明胶水溶液中分散均匀得到溶液A,将溶液A与有机溶剂、表面活性剂混匀乳化得到乳化液,然后用交联剂固化,固液分离,真空冷冻干燥得到可降解吸附剂。
优选地,活性炭的粒径≤3μm。
优选地,活性炭是用甘蔗渣制备的活性炭。
上述活性炭的制备方法可以按照本领域常规生物质活性炭的制备方法制得。
优选地,活性炭、明胶的重量比为0.06-0.08:1。
优选地,溶液A、有机溶剂的体积比为12.5-20:80。
优选地,有机溶剂和表面活性剂的体积重量比为80ml:0.1-0.3g。
优选地,明胶和交联剂的重量比为1:0.15-0.2。
优选地,明胶水溶液的质量分数为5-8wt%。
优选地,于室温固化2.5-3h。
优选地,真空冷冻干燥的温度为-15至-10℃。
优选地,有机溶剂为乙酸乙酯、甲苯、液体石蜡中的至少一种。
优选地,表面活性剂为失水山梨醇脂肪酸酯、山梨醇酐单月桂酸酯聚氧乙烯醚中的至少一种。
上述失水山梨醇脂肪酸酯可以选用司盘80等,山梨醇酐单月桂酸酯聚氧乙烯醚可选用吐温20等。
优选地,交联剂为甲醛、戊二醛中的至少一种。
上述水均为去离子水。
本发明还提出了一种可降解吸附剂,按照上述可降解吸附剂的制备方法制得。
本发明还提出了上述可降解吸附剂在甘蔗糖液除杂脱色中的应用。
有益效果:
本发明选用明胶水溶液和适宜粒径的活性炭混匀,然后制备乳化液,并用交联剂交联固化得到明胶微球,明胶分子链上含有丰富的氨基、羧基和羟基,具有一定的吸附性能,在明胶微球中引入活性炭,使得明胶微球表面呈粗糙多孔状态,进而大幅提高其吸附性能,经冷冻干燥使得微球具有交联网络与活性炭的多孔状态相互配合,进一步提高本发明的吸附性能;另外将明胶微球化,改善其遇水易溶胀的问题,提高吸附性能的稳定性,使得本发明可以重复利用;还有明胶可以自然降解,不会污染环境;选用甘蔗渣制备活性炭,可以解决在制糖过程中,剩余甘蔗渣容易污染环境的问题,可降低原料成本。发明人惊喜的发现,本发明可以很好的去除甘蔗糖液中杂质和色素,脱盐脱色,解决残硫问题。
具体实施方式
下面,通过具体实施例对本发明的技术方案进行详细说明。
实施例1
一种可降解吸附剂的制备方法,包括如下步骤:将0.06g粒径≤3μm的活性炭(甘蔗渣制备的活性炭)加入20ml质量分数为5wt%明胶水溶液中,超声分散均匀得到溶液A,
将20ml溶液A、0.1g司盘80加入80ml乙酸乙酯中,混匀乳化2h得到乳化液,然后滴加0.2g戊二醛于室温固化2.5h,过滤,用乙醇、水依次洗涤4次,然后于-10℃真空冷冻干燥得到可降解吸附剂,其平均粒径为61μm。
实施例2
一种可降解吸附剂的制备方法,包括如下步骤:将0.08g粒径≤3μm的活性炭(甘蔗渣制备的活性炭)加入12.5ml质量分数为8wt%明胶水溶液中,超声分散均匀得到溶液A,
将12.5ml溶液A、0.3g司盘80加入80ml甲苯中,混匀乳化2h得到乳化液,然后滴加0.15g戊二醛于室温固化3h,过滤,用乙醇、水依次洗涤4次,然后于-15℃真空冷冻干燥得到可降解吸附剂,其平均粒径为70μm。
实施例3
一种可降解吸附剂的制备方法,包括如下步骤:将0.07g粒径≤3μm的活性炭(甘蔗渣制备的活性炭)加入16ml质量分数为6.5wt%明胶水溶液中,超声分散均匀得到溶液A,
将16ml溶液A、0.2g司盘80加入80ml液体石蜡中,混匀乳化2h得到乳化液,然后滴加0.17g戊二醛于室温固化2.8h,过滤,用乙醇、水依次洗涤4次,然后于-13℃真空冷冻干燥得到可降解吸附剂,其平均粒径为65μm。
对比例1
一种明胶微球的制备方法为:将16ml质量分数为6.5wt%明胶水溶液、0.2g司盘80加入80ml液体石蜡中,混匀乳化2h得到乳化液,然后滴加0.17g戊二醛于室温固化2.8h,过滤,用乙醇、水依次洗涤4次,然后于-13℃真空冷冻干燥即得,其平均粒径为50μm。
对比例2
同实施例3的活性炭。
实验1
取甘蔗混合汁过200目滤网,然后加入磷酸(其浓度为300mg/L),用石灰乳调节pH=6.6,等分成6份,每份均为100ml,
取5份均加热至50℃,然后分别加入实施例1-3、对比例1-2(实施例1-3和对比例1-2的质量分数均为2wt%)分别记为实验组1-3、对照组1-2,然后用石灰乳调节pH=7.0,加热至90℃,再加入聚丙酰胺(每组浓度均为2mg/L),保温沉降,固液分离得到清汁;
第6份通入20ml SO2(记为对照组3),加热至90℃,再加入聚丙酰胺(浓度为2mg/L),保温沉降,固液分离得到清汁。
按照《甘蔗制糖化学管理分析方法》检测混合汁和清汁的纯度差△G.P、脱色率,结果如表1所示。
△G.P=清汁的重力纯度-混合汁的重力纯度。
脱色率=(IU清汁-IU混合汁)/IU混合汁*100%,其中,于420nm检测色值IU。
表1检测结果
| 分组 | 纯度差% | 脱色率% |
| 实验组1 | 2.7 | 73 |
| 实验组2 | 2.7 | 75 |
| 实验组3 | 2.8 | 74 |
| 对照组1 | 0.8 | 40 |
| 对照组2 | 0.4 | 28 |
| 对照组3 | 1.3 | 50 |
由表1可以看出,经本发明处理后,甘蔗混合汁和清汁的纯度差、脱色率均优于单独的明胶微球、活性炭和亚硫酸法,且没有残硫问题;本发明可以很好的去除甘蔗糖液中杂质和色素。
实验2
取实施例3制得的吸附剂,按照实验1的方法处理得到清汁;并经3次吸附-脱附循环,考察每次获得清汁的纯度差和脱色率,结果如表2所示。
脱附处理方法为:将使用后的吸附剂加入5g/L的氢氧化钠溶液中,于20-25℃保温振荡40min即可。
表2循环性能
由上表可以看出:本发明经3次吸附-脱附循环,清汁的纯度差和脱色率均优于亚硫酸法(如实验1中对照组3的数据),本发明可以重复使用。
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。
Claims (10)
1.一种可降解吸附剂的制备方法,其特征在于,包括如下步骤:将活性炭在明胶水溶液中分散均匀得到溶液A,将溶液A与有机溶剂、表面活性剂混匀乳化得到乳化液,然后用交联剂固化,固液分离,真空冷冻干燥得到可降解吸附剂。
2.根据权利要求1所述可降解吸附剂的制备方法,其特征在于,活性炭的粒径≤3μm;优选地,活性炭是用甘蔗渣制备的活性炭。
3.根据权利要求1或2所述可降解吸附剂的制备方法,其特征在于,活性炭、明胶的重量比为0.06-0.08:1。
4.根据权利要求1-3任一项所述可降解吸附剂的制备方法,其特征在于,溶液A、有机溶剂的体积比为12.5-20:80;优选地,有机溶剂和表面活性剂的体积重量比为80ml:0.1-0.3g;优选地,明胶和交联剂的重量比为1:0.15-0.2。
5.根据权利要求1-4任一项所述可降解吸附剂的制备方法,其特征在于,明胶水溶液的质量分数为5-8wt%。
6.根据权利要求1-5任一项所述可降解吸附剂的制备方法,其特征在于,于室温固化2.5-3h。
7.根据权利要求1-6任一项所述可降解吸附剂的制备方法,其特征在于,真空冷冻干燥的温度为-15至-10℃。
8.根据权利要求1-7任一项所述可降解吸附剂的制备方法,其特征在于,有机溶剂为乙酸乙酯、甲苯、液体石蜡中的至少一种;优选地,表面活性剂为失水山梨醇脂肪酸酯、山梨醇酐单月桂酸酯聚氧乙烯醚中的至少一种;优选地,交联剂为甲醛、戊二醛中的至少一种。
9.一种可降解吸附剂,其特征在于,按照权利要求1-8任一项所述可降解吸附剂的制备方法制得。
10.一种如权利要求9所述可降解吸附剂在甘蔗糖液除杂脱色中的应用。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011381180.4A CN112642404A (zh) | 2020-12-01 | 2020-12-01 | 一种可降解吸附剂及其制备方法、应用 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011381180.4A CN112642404A (zh) | 2020-12-01 | 2020-12-01 | 一种可降解吸附剂及其制备方法、应用 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112642404A true CN112642404A (zh) | 2021-04-13 |
Family
ID=75349862
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011381180.4A Pending CN112642404A (zh) | 2020-12-01 | 2020-12-01 | 一种可降解吸附剂及其制备方法、应用 |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112642404A (zh) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR777364A (fr) * | 1934-08-06 | 1935-02-18 | Charbon structural activé et procédé pour le fabriquer | |
| DE3015439A1 (de) * | 1980-04-22 | 1981-10-29 | Bayer Ag, 5090 Leverkusen | Verfahren zur herstellung von im waessrigen system zerfallendenaktivkohlegranulaten und deren verwendung |
| CN1229367A (zh) * | 1996-07-22 | 1999-09-22 | 亘起物产有限会社 | 新的吸附剂 |
| US5972121A (en) * | 1997-04-09 | 1999-10-26 | Rohm And Haas Company | Decolorization of sugar syrups using functionalized adsorbents |
| CN1956918A (zh) * | 2004-05-26 | 2007-05-02 | 大塚食品株式会社 | 活性炭组合物和使用该活性炭组合物的液状物的脱色方法 |
| RU2365626C1 (ru) * | 2006-03-24 | 2009-08-27 | Афанасий Моисеевич Ким | Способ производства сахара |
| CN107384630A (zh) * | 2017-06-28 | 2017-11-24 | 常州建轩纺织品有限公司 | 一种活性染料用吸附型生物酶皂洗剂的制备方法 |
-
2020
- 2020-12-01 CN CN202011381180.4A patent/CN112642404A/zh active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR777364A (fr) * | 1934-08-06 | 1935-02-18 | Charbon structural activé et procédé pour le fabriquer | |
| DE3015439A1 (de) * | 1980-04-22 | 1981-10-29 | Bayer Ag, 5090 Leverkusen | Verfahren zur herstellung von im waessrigen system zerfallendenaktivkohlegranulaten und deren verwendung |
| CN1229367A (zh) * | 1996-07-22 | 1999-09-22 | 亘起物产有限会社 | 新的吸附剂 |
| US5972121A (en) * | 1997-04-09 | 1999-10-26 | Rohm And Haas Company | Decolorization of sugar syrups using functionalized adsorbents |
| CN1956918A (zh) * | 2004-05-26 | 2007-05-02 | 大塚食品株式会社 | 活性炭组合物和使用该活性炭组合物的液状物的脱色方法 |
| RU2365626C1 (ru) * | 2006-03-24 | 2009-08-27 | Афанасий Моисеевич Ким | Способ производства сахара |
| CN107384630A (zh) * | 2017-06-28 | 2017-11-24 | 常州建轩纺织品有限公司 | 一种活性染料用吸附型生物酶皂洗剂的制备方法 |
Non-Patent Citations (7)
| Title |
|---|
| FAREEDA HAYEEYE ET.AL: "Preparation and Adsorption Study of Gelatin/Activated Carbon Composite Bead Form", 《ADVANCED MATERIALS RESEARCH》 * |
| 冯淑娟等: "活性炭负载壳聚糖的制备及其对糖汁清净性能研究", 《食品工业科技》 * |
| 方红英等: "乙酰半胱氨酸活性炭微囊的制备工艺筛选", 《中国药房》 * |
| 李雪珍等: "壳聚糖-活性炭协同对蔗汁的脱色效果", 《中国糖料》 * |
| 杨桂馥 罗瑜编著, 天津科学技术出版社 * |
| 钟碧疆等: "天然有机高分子絮凝剂在蔗汁澄清中的应用", 《食品科技》 * |
| 顾学裘: "《药物制剂新剂型选编》", 31 January 1984, 人民卫生出版社 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE3852233T2 (de) | Multizellulare Zellulosepartikel und Verfahren zu ihrer Herstellung. | |
| US11021588B2 (en) | Method for producing porous cellulose medium | |
| US5569740A (en) | Deproteinized natural rubber latex and its production process | |
| DE2510374C3 (de) | Verfahren zum Klären einer wässrigen Lösung von Xanthangummi | |
| CH439756A (de) | Verfahren zur Herstellung von hydrophilen Polymeräthern in Form von Gelkörnern | |
| JPS603478B2 (ja) | キサンタンゴムの処理法 | |
| EP3279219B1 (en) | Method for producing porous cellulose medium | |
| CN109070054B (zh) | 多孔性纤维素介质的制造方法 | |
| CN104450799A (zh) | 一种制备固体山梨醇并联产果葡糖浆的生产工艺 | |
| DE2351520C2 (de) | Verfahren zur Konzentrierung von Suspensionen von thermisch gelierbaren Polysacchariden | |
| DE69410763T2 (de) | Microsphäre und Verfahren zu deren Herstellung | |
| RU2119758C1 (ru) | Способ получения целлюлозосодержащего зернового экстракта | |
| CN112642404A (zh) | 一种可降解吸附剂及其制备方法、应用 | |
| EP1748051A1 (de) | Monodisperse Kationenaustauscher | |
| DE3687807T2 (de) | Sphaerische poly(alpha-aminosaeure)koerner und verfahren zu deren herstellung. | |
| US4937081A (en) | Process for producing porous, spherical particles | |
| EP0370911A1 (fr) | Solutions liquides concentrées de polysaccharides | |
| CN113083253A (zh) | 一种提取维生素b12用弱酸阳树脂及其合成方法 | |
| CN112642405A (zh) | 一种可回收吸附剂及其制备方法、应用 | |
| US4478599A (en) | Method of continuously controlling crystal fines formation | |
| US3098044A (en) | Method of producing hydrous metal oxide sols | |
| NO142962B (no) | Gjenvinningsprosess for xantangummi. | |
| US3486844A (en) | Production of dense soda ash | |
| CN116102589A (zh) | 一种自玉米浸泡液中提取植酸钠的方法 | |
| US3197289A (en) | Modification of zinc hydrosulfite crystals by use of high molecular weight colloidal materials |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210413 |
|
| RJ01 | Rejection of invention patent application after publication |