CN113071039A - Preparation method of composite polyurethane condom - Google Patents
Preparation method of composite polyurethane condom Download PDFInfo
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- CN113071039A CN113071039A CN202110332819.8A CN202110332819A CN113071039A CN 113071039 A CN113071039 A CN 113071039A CN 202110332819 A CN202110332819 A CN 202110332819A CN 113071039 A CN113071039 A CN 113071039A
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- drying
- tank
- temperature
- soaking
- condom
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- 229920002635 polyurethane Polymers 0.000 title claims abstract description 37
- 239000004814 polyurethane Substances 0.000 title claims abstract description 37
- 239000002131 composite material Substances 0.000 title claims abstract description 15
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 94
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000002791 soaking Methods 0.000 claims abstract description 23
- 238000007598 dipping method Methods 0.000 claims abstract description 17
- 238000005406 washing Methods 0.000 claims abstract description 6
- 238000007654 immersion Methods 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 21
- 239000003795 chemical substances by application Substances 0.000 claims description 16
- 239000003292 glue Substances 0.000 claims description 15
- 238000005470 impregnation Methods 0.000 claims description 9
- 150000007942 carboxylates Chemical group 0.000 claims description 8
- 239000000839 emulsion Substances 0.000 claims description 8
- 239000000080 wetting agent Substances 0.000 claims description 8
- 239000002518 antifoaming agent Substances 0.000 claims description 6
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 5
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 2
- 230000001680 brushing effect Effects 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 239000013530 defoamer Substances 0.000 claims description 2
- 239000011521 glass Substances 0.000 claims description 2
- 238000000643 oven drying Methods 0.000 claims description 2
- 238000005201 scrubbing Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 9
- 239000000463 material Substances 0.000 description 30
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 8
- 238000007605 air drying Methods 0.000 description 7
- 238000009472 formulation Methods 0.000 description 5
- 239000004970 Chain extender Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 208000015181 infectious disease Diseases 0.000 description 3
- 229920002873 Polyethylenimine Polymers 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- KPUWHANPEXNPJT-UHFFFAOYSA-N disiloxane Chemical class [SiH3]O[SiH3] KPUWHANPEXNPJT-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012948 isocyanate Substances 0.000 description 2
- 150000002513 isocyanates Chemical class 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- 125000005647 linker group Chemical group 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000001568 sexual effect Effects 0.000 description 2
- 229920002545 silicone oil Polymers 0.000 description 2
- PTBDIHRZYDMNKB-UHFFFAOYSA-N 2,2-Bis(hydroxymethyl)propionic acid Chemical compound OCC(C)(CO)C(O)=O PTBDIHRZYDMNKB-UHFFFAOYSA-N 0.000 description 1
- JVYDLYGCSIHCMR-UHFFFAOYSA-N 2,2-bis(hydroxymethyl)butanoic acid Chemical compound CCC(CO)(CO)C(O)=O JVYDLYGCSIHCMR-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 208000035432 Unintended pregnancy Diseases 0.000 description 1
- -1 acetylene glycol Chemical compound 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 210000000936 intestine Anatomy 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 125000005375 organosiloxane group Chemical group 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000035935 pregnancy Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/02—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
- B29C41/14—Dipping a core
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C33/00—Moulds or cores; Details thereof or accessories therefor
- B29C33/56—Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
- B29C33/60—Releasing, lubricating or separating agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/02—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
- B29C41/22—Making multilayered or multicoloured articles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/34—Component parts, details or accessories; Auxiliary operations
- B29C41/46—Heating or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2075/00—Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/753—Medical equipment; Accessories therefor
- B29L2031/7538—Condoms
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Orthopedics, Nursing, And Contraception (AREA)
Abstract
The invention discloses a preparation method of a composite polyurethane condom, relating to the technical field of medical appliances, and comprising the following steps: (1) washing the die; (2) a hot immersion water tank; (3) primary drying; (4) soaking a first tank; (5) secondary drying; (6) soaking a second tank; (7) drying for three times; (8) soaking a third tank; (9) drying for four times; (10) soaking a No. four tank; (11) drying for five times; (12) curling; (13) drying for six times; (14) demoulding; (15) and (5) washing the die. According to the invention, the condom with the structure comprising the release layer, the polyurethane inner layer, the linking layer and the polyurethane outer layer from inside to outside is prepared by sequentially dipping the first groove, the second groove, the third groove and the fourth groove.
Description
The technical field is as follows:
the invention relates to the technical field of medical instruments, in particular to a preparation method of a composite polyurethane condom.
Background art:
condoms are a barrier type device that can be used during sexual intercourse to reduce the risk of sexually transmitted infections and involuntary pregnancy for women. The condom material is mainly latex, plastic or sheepskin film, both of which can protect the user from sexually transmitted infections during sexual intercourse, but since sheepskin condoms are made of material from the intestines of sheep, which have tiny openings, like human skin, they can only prevent unintended pregnancy, but cannot avoid sexually transmitted infections.
At present, domestic enterprises have mastered the preparation technology of condoms, but a certain gap still exists between the aspect of preparing ultrathin condoms and developed countries, and the softness, water resistance and alcohol resistance of the condoms are also required to be improved. Although a plurality of existing Chinese patents disclose methods for preparing condoms, the water resistance and the alcohol resistance of the condoms are not tested, or the water resistance and the alcohol resistance of the condoms are not good, so that the comprehensive performance of the condoms needs to be optimized by screening raw materials for preparing the condoms, designing the structures of the condoms and improving the preparation method of the condoms, and the use quality of the condoms needs to be improved.
The invention content is as follows:
the technical problem to be solved by the invention is to provide a preparation method of a composite polyurethane condom, which is used for preparing a high-performance condom by using simple and easy process operation, simultaneously reducing the preparation cost and being suitable for large-scale production.
The technical problem to be solved by the invention is realized by adopting the following technical scheme:
a preparation method of a composite polyurethane condom comprises the following steps:
(1) washing the die: repeatedly scrubbing the mould by using a brush;
(2) a hot immersion water tank: the temperature of the hot water tank is 50-100 ℃, the time of soaking the hot water tank is 3-10s, and the conductivity of water used in the hot water tank is less than or equal to 40 mu s-cm;
(3) primary drying: natural drying, air-blowing drying or oven drying is adopted, and the drying time is 5-20 s;
(4) soaking in a first tank: the first tank is a release agent blend, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(5) secondary drying: drying at 50-120 deg.C for 1-10 min;
(6) soaking in a second tank: the second tank is sulfonate type polyurethane emulsion, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(7) and (3) drying for three times: drying at 50-120 deg.C for 1-10 min;
(8) soaking in a third tank: the third tank is a linking agent blend, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(9) and (3) drying for four times: drying at 50-120 deg.C for 1-10 min;
(10) soaking in a No. four tank: the fourth tank is carboxylate polyurethane emulsion, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(11) and (4) five times of drying: drying at 80-140 deg.C for 1-10 min;
(12) edge curling: curling the glue film formed on the die;
(13) and (3) six times of drying: drying at 80-140 deg.C for 15-50 min;
(14) demoulding: brushing the product off the mold by using a brush roll;
(15) washing the die: the mold is repeatedly scrubbed by a hairbrush.
The mould is made of glass.
The temperature of the hot water tank is preferably 65-80 ℃.
The temperature of the glue tank of the first soaking tank is preferably 25 +/-5 ℃.
The temperature of the secondary drying is preferably 80 ℃. + -. 10 ℃.
The temperature of the glue tank of the second soaking tank is preferably 25 +/-5 ℃.
The temperature of the tertiary drying is preferably 80 ℃. + -. 10 ℃.
The temperature of the glue tank of the third soaking tank is preferably 25 +/-5 ℃.
The temperature of the four drying times is preferably 80 ℃. + -. 10 ℃.
The temperature of the glue tank of the No. four soaking tank is preferably 25 +/-5 ℃.
The temperature of the five drying times is preferably 100 ℃. + -. 10 ℃.
The temperature of the six drying is preferably 100 ℃. + -. 10 ℃.
The release agent blend in the first tank consists of a release agent, a defoaming agent, a wetting agent and water, and the dipping thickness can be ignored.
The sulfonate polyurethane emulsion in the second tank consists of sulfonate polyurethane and deionized water, the solid content is 10-35%, and the thickness of a film generated after dipping is 5-20 mu m.
The linker blend in tank three consists of linker, defoamer, wetting agent and water, and the impregnation thickness is negligible.
The carboxylate polyurethane emulsion in the fourth tank consists of carboxylate polyurethane and deionized water, the solid content is 10-35%, and the thickness of a film generated after dipping is 5-20 mu m.
The release agent is one or a mixture of more than two of calcium stearate, straight-chain alkane, hydroxyl silicone oil and dimethyl silicone oil, and the content is 1-15%, preferably 5-10%, and more preferably 7 +/-2% by mass.
The molecule chain segment of the sulfonate type polyurethane at least comprises a hydrophilic group with a sulfonate structure, the hydrophilic group provides a micromolecule chain extender, and the micromolecule chain extender is selected from one or a mixture of more than two of the following compounds a, b and c:
the linking agent is one or a mixture of more than two of organic siloxane, polyethylenimine, blocked isocyanate and polycarbodiimide, and the content is 0-0.5 percent by mass.
The defoaming agent is one or a mixture of more than two of organosilicon defoaming agent, organic fluorine defoaming agent and mineral oil defoaming agent, and the content is 0.01-0.1% by mass.
The wetting agent is one or a mixture of two of an organic silicon wetting agent and an acetylene glycol wetting agent, and the content of the wetting agent is 0.01-0.5% by mass.
The molecular chain segment of the carboxylate polyurethane at least comprises a hydrophilic group with a carboxylate structure, the hydrophilic group is provided for a small molecular chain extender, triethylamine is used for neutralization, and the small molecular chain extender is selected from one or a mixture of two of 2, 2-dimethylolpropionic acid (DMPA) and 2, 2-dimethylolbutyric acid (DMBA).
The interlinkage layer in the condom structure has the function of recoating effect, and because the compatibility of two polyurethanes with different structures adopted by the polyurethane inner layer and the polyurethane outer layer is poor, the interlinkage agent blend is required to prevent the layering phenomenon.
Because the application of the linking agent is directly related to whether the condom with the structure can be molded as expected and the using quality of the condom, the invention adopts the polyallylthiourethane as the linking agent besides the organic siloxane, the polyaziridine, the blocked isocyanate and the polycarbodiimide as the linking agent, and can further optimize the comprehensive performance of the condom.
The linking agent is poly (N-allyl-O-isobutyl-thiourethane) and has the weight-average molecular weight of (1-10) multiplied by 104。
The invention has the beneficial effects that:
(1) according to the invention, the condom with the structure comprising the release layer, the polyurethane inner layer, the linking layer and the polyurethane outer layer from inside to outside is prepared by sequentially dipping the first groove, the second groove, the third groove and the fourth groove, so that the preparation method is simple, has no special equipment requirement, has definite control parameters of preparation conditions, and is suitable for large-scale production, and the composition of the dipping solution is clear.
(2) The condom prepared by the invention has good flexibility, the modulus is less than or equal to 2MPa, the elongation at break reaches 500 percent, the burst volume is more than or equal to 8L, and the burst pressure is more than or equal to 5.0 kPa; the water resistance is good, the ring-shaped breaking force is more than or equal to 20N when the raw materials are boiled in pure water for 1 hour at 50 ℃; the alcohol resistance is good, the wine is taken out after being soaked in 75% alcohol for 5min, and the wine is immediately wiped dry, and the ring pulling breaking force is more than or equal to 10N.
The specific implementation mode is as follows:
in order to make the technical means, the creation characteristics, the achievement purposes and the effects of the invention easy to understand, the invention is further described with the specific embodiments.
Example 1
The formula is as follows:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 5s |
First tank material temperature | 30±2℃ | 35s |
Temperature of material in second groove | 30±2℃ | 35s |
Temperature of material in third groove | 30±2℃ | 35s |
Temperature of material in No. four groove | 30±2℃ | 35s |
Primary drying temperature | Natural air drying | 14s |
Secondary drying temperature | 80±5℃ | 8min |
Third drying temperature | 80±5℃ | 8min |
Fourth drying temperature | 80±5℃ | 8min |
Five times of drying temperature | 80±5℃ | 8min |
Six times of drying temperature | 80±5℃ | 35min |
Example 2 formulation:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 3s |
First tank material temperature | 30±2℃ | 20s |
Temperature of material in second groove | 30±2℃ | 20s |
Temperature of material in third groove | 30±2℃ | 20s |
Temperature of material in No. four groove | 30±2℃ | 20s |
Primary drying temperature | Natural air drying | 8s |
Secondary drying temperature | 110±5℃ | 4min |
Third drying temperature | 110±5℃ | 4min |
Fourth drying temperature | 110±5℃ | 4min |
Five times of drying temperature | 110±5℃ | 4min |
Six times of drying temperature | 110±5℃ | 19min |
Example 3 formulation:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 5s |
First tank material temperature | 30±2℃ | 35s |
Temperature of material in second groove | 30±2℃ | 35s |
Temperature of material in third groove | 30±2℃ | 35s |
Temperature of material in No. four groove | 30±2℃ | 35s |
Primary drying temperature | Natural air drying | 14s |
Secondary drying temperature | 80±5℃ | 8min |
Third drying temperature | 80±5℃ | 8min |
Fourth drying temperature | 80±5℃ | 8min |
Five times of drying temperature | 80±5℃ | 8min |
Six times of drying temperature | 80±5℃ | 35min |
Example 4 formulation:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 3s |
First tank material temperature | 30±2℃ | 20s |
Temperature of material in second groove | 30±2℃ | 20s |
Temperature of material in third groove | 30±2℃ | 20s |
Temperature of material in No. four groove | 30±2℃ | 20s |
Primary drying temperature | Natural air drying | 8s |
Secondary drying temperature | 110±5℃ | 4min |
Third drying temperature | 110±5℃ | 4min |
Fourth drying temperature | 110±5℃ | 4min |
Five times of drying temperature | 110±5℃ | 4min |
Six times of drying temperature | 110±5℃ | 19min |
Example 5 formulation:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 5s |
First tank material temperature | 30±2℃ | 35s |
Temperature of material in second groove | 30±2℃ | 35s |
Temperature of material in third groove | 30±2℃ | 35s |
Temperature of material in No. four groove | 30±2℃ | 35s |
Primary drying temperature | Natural air drying | 14s |
Secondary drying temperature | 80±5℃ | 8min |
Third drying temperature | 80±5℃ | 8min |
Fourth drying temperature | 80±5℃ | 8min |
Five times of drying temperature | 80±5℃ | 8min |
Six times of drying temperature | 80±5℃ | 35min |
Example 6 formulation:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 3s |
First tank material temperature | 30±2℃ | 20s |
Temperature of material in second groove | 30±2℃ | 20s |
Temperature of material in third groove | 30±2℃ | 20s |
Temperature of material in No. four groove | 30±2℃ | 20s |
Primary drying temperature | Natural air drying | 8s |
Secondary drying temperature | 110±5℃ | 4min |
Third drying temperature | 110±5℃ | 4min |
Fourth drying temperature | 110±5℃ | 4min |
Five times of drying temperature | 110±5℃ | 4min |
Six times of drying temperature | 110±5℃ | 19min |
Example 7
The organosiloxane XR500 from slot three in example 6 was replaced with poly (N-allyl-O-isobutyl-thiourethane) prepared by the following steps: adding 17.3g N-allyl-O-isobutyl-thiourethane and 0.8g benzoyl peroxide into 250mL tetrahydrofuran, carrying out heat preservation reaction for 5h under the reflux state, slowly adding water under stirring until no white precipitate is continuously separated out, filtering, drying filter residues, and crushing into powder to obtain the poly (N-allyl-O-isobutyl-thiourethane).
The formula is as follows:
the technological parameters are as follows:
item | Parameter(s) | Drying/impregnation time |
Temperature of hot water tank | 75±5℃ | 3s |
First tank material temperature | 30±2℃ | 20s |
Temperature of material in second groove | 30±2℃ | 20s |
Temperature of material in third groove | 30±2℃ | 20s |
Temperature of material in No. four groove | 30±2℃ | 20s |
Primary drying temperature | Natural air drying | 8s |
Secondary drying temperature | 110±5℃ | 4min |
Third drying temperature | 110±5℃ | 4min |
Fourth drying temperature | 110±5℃ | 4min |
Five times of drying temperature | 110±5℃ | 4min |
Six times of drying temperature | 110±5℃ | 19min |
The condom with the thickness of 25 microns +/-2 microns is prepared by respectively utilizing the formula and the process parameters, and the performance of the condom is compared with that of a commercially available product, wherein the performance comprises thickness, modulus, elongation at break, burst volume, burst pressure, water resistance and alcohol resistance.
The modulus was tested with reference to HG/T3321-.
The tests of thickness, elongation at break, burst volume and burst pressure were referenced to HG/T5456-2018.
And (3) testing water resistance: boiling in pure water at 50 deg.C for 1 hr, and ring pulling force is not less than 20N.
Testing alcoholic strength: soaking in 75% alcohol for 5min, taking out, and immediately wiping to dry, wherein the ring pull breaking force is not less than 10N.
The test results are shown in the following table.
As can be seen from the table 1, the condom prepared by the invention is far superior to the current commercial known condom in softness, water resistance and alcohol resistance; and the self-made poly (N-allyl-O-isobutyl-thiourethane) is adopted as a linking agent, so that the comprehensive performance of the condom can be further optimized.
The foregoing shows and describes the general principles and broad features of the present invention and advantages thereof. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (10)
1. A preparation method of a compound polyurethane condom is characterized in that: the method comprises the following steps:
(1) washing the die: repeatedly scrubbing the mould by using a brush;
(2) a hot immersion water tank: the temperature of the hot water tank is 50-100 ℃, the time of soaking the hot water tank is 3-10s, and the conductivity of water used in the hot water tank is less than or equal to 40 mu s-cm;
(3) primary drying: natural drying, air-blowing drying or oven drying is adopted, and the drying time is 5-20 s;
(4) soaking in a first tank: the first tank is a release agent blend, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(5) secondary drying: drying at 50-120 deg.C for 1-10 min;
(6) soaking in a second tank: the second tank is sulfonate type polyurethane emulsion, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(7) and (3) drying for three times: drying at 50-120 deg.C for 1-10 min;
(8) soaking in a third tank: the third tank is a linking agent blend, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(9) and (3) drying for four times: drying at 50-120 deg.C for 1-10 min;
(10) soaking in a No. four tank: the fourth tank is carboxylate polyurethane emulsion, the temperature of the glue tank is 0-40 ℃, and the dipping time is 10-40 s;
(11) and (4) five times of drying: drying at 80-140 deg.C for 1-10 min;
(12) edge curling: curling the glue film formed on the die;
(13) and (3) six times of drying: drying at 80-140 deg.C for 15-50 min;
(14) demoulding: brushing the product off the mold by using a brush roll;
(15) washing the die: the mold is repeatedly scrubbed by a hairbrush.
2. The method of making a composite polyurethane condom of claim 1, wherein: the mould is made of glass.
3. The method of making a composite polyurethane condom of claim 1, wherein: the temperature of the hot water tank is preferably 65-80 ℃.
4. The method of making a composite polyurethane condom of claim 1, wherein: the temperature of the glue grooves of the first soaking groove, the second soaking groove, the third soaking groove and the fourth soaking groove is preferably 25 +/-5 ℃.
5. The method of making a composite polyurethane condom of claim 1, wherein: the temperature of the secondary drying, the tertiary drying and the quartic drying is preferably 80 +/-10 ℃.
6. The method of making a composite polyurethane condom of claim 1, wherein: the temperature of the five-time drying and the six-time drying is preferably 100 ℃ +/-10 ℃.
7. The method of making a composite polyurethane condom of claim 1, wherein: the release agent blend in the first tank consists of a release agent, a defoaming agent, a wetting agent and water, and the dipping thickness can be ignored.
8. The method of making a composite polyurethane condom of claim 1, wherein: the sulfonate polyurethane emulsion in the second tank consists of sulfonate polyurethane and deionized water, the solid content is 10-35%, and the thickness of a film generated after dipping is 5-20 mu m.
9. The method of making a composite polyurethane condom of claim 1, wherein: the linker blend in tank three consists of linker, defoamer, wetting agent and water, and the impregnation thickness is negligible.
10. The method of making a composite polyurethane condom of claim 1, wherein: the carboxylate polyurethane emulsion in the fourth tank consists of carboxylate polyurethane and deionized water, the solid content is 10-35%, and the thickness of a film generated after dipping is 5-20 mu m.
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