TWI305540B - Method for preparing formed polyurethane foam materials and formed polyurethane foam materials therefrom - Google Patents

Method for preparing formed polyurethane foam materials and formed polyurethane foam materials therefrom Download PDF

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TWI305540B
TWI305540B TW94111271A TW94111271A TWI305540B TW I305540 B TWI305540 B TW I305540B TW 94111271 A TW94111271 A TW 94111271A TW 94111271 A TW94111271 A TW 94111271A TW I305540 B TWI305540 B TW I305540B
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foam
polyurethane
polyurethane foam
molded
patent application
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TW94111271A
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TW200635990A (en
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Jung Shun Ou
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Tu Chunghsien
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Description

l3〇5540 九、發明說明: 【發明所屬之技術領域】 本發明是關於-種無接縫(seam㈣解_、罩杯、軍頂及胸罩及其他 服裝所用物件卿之相類物品。本發明之方法特別適用在模製無接縫利用脂肪族 異氰酸合物衫元醇之聚合作騎產生之„聚氨脂發紐所製成之胸罩 之罩杯。 【先前技術】L3〇5540 IX. Description of the Invention: [Technical Field of the Invention] The present invention relates to a kind of seamless article (seam solution, cup, military top and bra, and other items used in clothing). The method of the present invention It is especially suitable for the cups of bras made of polyurethane foam made by the jointing of the aliphatic isocyanate compound.

在胸罩及其他具有成形胸部罩杯之服裝之製備上,常需使用可以經常保持原 形,但可聽繼娜Η罐糊娜_。❹卜,她輸及彈 _必須在人工及機器絲之下仍能維持。此外,胸罩罩杯必須具備充分之孔隙 率及透氣性,以提高穿載者之舒適度。 傳統之胸料㈣是由填充纖維(f_)㈣,哺製方式作成不同厚度 之罩杯。習知技術之製法缺點乃是在罩頂處厚度較薄,結果導致在人工及機器洗 條以後無峨原㈣克服此細咖題,—般編在罩頂處縫線加以解 决。不過縫線的方式無法滿足近來在無躺鮮罩杯流行之需求。 種改良的胸罩罩杯製法發表在美國專利第4,〇25,597號,⑽年$月% 日頒予“hiS_mot。)。該發鶴以型模恤祕⑻製法以—哉塑性 樹脂均镇柿„纖特料之巾,紐瓶_置於麵模㈤⑽⑷中 加熱至高於靖脂之魏溫紅上,製縣杯。這财《在該纖树料内形成 熱塑_脂均勾(麵ogen咖)的分布。且使用這種方法製成均一柔軟度及彈 性之草杯,财料。另—個義乃是該細必職確控·鴻含量。 太多樹脂,則會製成僵硬的罩杯 口入 聯杯缺乏㈣生。反之,如果樹脂含量太少,則可能 5 1305540 因為洗滌而導致變形,無法維持其形狀。 另-種製備胸罩罩杯的方法乃是使用熱固性聚氨基甲酸醋(p〇lyurethane)發 /包體例如美國專利第4,25〇,137號(1981年2月1〇日頒予Walter Riedler)所示 . 之方法。其製備步驟包括:從—大塊聚氨基曱酸醋塊狀發泡體上,載下-片聚氨 ‘ 基曱喊發泡體’置於二相合模具,即加熱中之-公模具及-母模具之中。依其 、 專利*明書之記載,罐具係加熱至35G.45G°F。對該聚氨基甲麵發泡體材料 施加壓力’約每平方英叶6〇碎(對模具表面),對聚氨基甲酸酿發泡體施預熱, # 咖度約4〇0 F。同時加壓及加熱約60秒,但實際上之反應期間仍依該聚氨基曱酸 酉曰發泡體片之厚度而異。由於聚氨基甲酸醋發泡體材料之低熱傳導率,厚度較大 之發泡體片常需使用較長的製程時間,才能在該聚氨基甲酸醋發泡體材料中央部 伤產生足夠的飾。上賴處理可麟致聚錄甲麟麟之化學鏈產生斷裂 (dissociatiGn)。所製成之產品之物理雜因嘯著降低,且在使用躺聚氨基甲 酸酯發泡體會加速變黃。 使用芳香族聚氨基甲酸醋發泡體明顯之缺點為其變色之特性。如所周知,芳 • 魏聚乱基?_旨發泡體暴露於光線,尤其是紫外線下會變黃。在Kiyotake之歐 州專利λ σ案G,473,1〇7號中,揭示了—種利削旨肪族氰自㈣旨以解決上述問題的 方法。籍明之步驟包括對一多元醇(p〇ly〇1)加入一脂肪族異氣酸輯(為m.6 仏氫乳基當量)及水(為多元醇重量的〇4_5百分比),在觸媒存在下進行反應。 亥方法可產生;F會變黃的脂肪麟氨基旨發泡體。不過,該脂肪族聚氨基甲 酸醋發泡體在其大部份的結構中,含有封閉的小胞(cdl),其原因為該脂肪族異 氰酸S曰“團的低反應速率,導致小胞無法破裂。這種封閉的小胞結構位在聚氨 6 1305540 熱壓成型上的困難,使其熱壓成型需 所製成的發泡體胸罩墊片由於為含有 基甲酸酯發泡體中,導致較慢的散熱效率及 使用較高的熱成形溫度及較長的處理時間。 殘留小胞的薄膜’只能提供有限的透氣性。 熱成形聚氨基甲酸醋胸草墊片另一種問題為其熱成形後所得的低孔隙率所 導致的繼氣性。Chen在其職年1G月23日第6,3_號瓣利中提供 一種製造具有錄空氣孔洞,而與上表面及下表面連通的聚氨基甲酸_罩塾片 的方法,㈣改良透紐。不過’這些空氣孔晴所製成的鮮罩杯的柔軟度及In the preparation of bras and other garments with shaped breast cups, it is often necessary to use them to maintain the original shape, but it can be heard. She, she lost and bombed _ must be maintained under the artificial and machine silk. In addition, bra cups must have sufficient porosity and breathability to improve wearer comfort. The traditional breast material (4) is made of filler fiber (f_) (4), and is made into cups of different thicknesses. The disadvantage of the conventional technique is that the thickness is thinner at the top of the cover, resulting in no artifacts after manual and machine washing (4) to overcome this fine problem, and the stitching at the top of the cover is solved. However, the way of suture can not meet the recent demand for the lack of lying cups. The improved bra cup method was published in U.S. Patent No. 4, No. 25,597, and (10) year (monthly) is awarded to "hiS_mot." The hair is made of a type of shirt (8). The special material towel, the new bottle _ is placed in the surface mold (five) (10) (4) heated to higher than the Wei Wen Wei Wenhong, the county cup. This fiscal "forms the distribution of thermoplastics in the fiber tree." And using this method to make a uniform softness and elasticity of the straw cup, the material. Another - meaning is that the fine must be controlled to control the content of Hong. Too much resin will make a stiff cup into the mouth. The cup is lacking (four) raw. On the other hand, if the resin content is too small, it is possible that 5 1305540 is deformed by washing and cannot maintain its shape. Another method of preparing a bra cup is to use a thermosetting urethane blister/encapsulated body such as U.S. Patent No. 4,25, 137 (issued to Walter Riedler on February 1, 1981). Show. The method. The preparation steps include: placing a - piece of polyaminating 'base foaming foam' on a bulk poly-amino citrate block foam, placing it in a two-phase mold, that is, heating - a male mold and - Among the mother molds. According to the patents and patents, the cans are heated to 35G.45G °F. The polyurethane foam material was subjected to a pressure of about 6 mash per square inch (to the surface of the mold), and the polyurethane foam was preheated, and the coffee was about 4 〇 0 F. At the same time, it is pressurized and heated for about 60 seconds, but the actual reaction period varies depending on the thickness of the polyurethane bismuth silicate foam sheet. Due to the low thermal conductivity of the polyurethane foam material, a relatively large thickness of the foam sheet often requires a long process time to produce sufficient decoration at the center of the polyurethane foam material. On the treatment of the lining, the chemical chain of Jia Linlin was broken (dissociatiGn). The physical impurities of the resulting product are reduced, and the use of the lying polyurethane foam accelerates yellowing. The obvious disadvantage of using an aromatic polyurethane foam is its discoloration characteristics. As is known, Fang Wei gathers the chaos? _The foam is exposed to light, especially under ultraviolet light. In the European Patent λ σ case G, 473, 1 〇 7 of Kiyotake, a method for solving the above problems is disclosed. The step of the Ming Dynasty includes adding an aliphatic iso-acid acid (for m.6 hydrazine base equivalent) and water (for 重量4_5 percentage of the weight of the polyol) to a polyol (p〇ly〇1). The reaction is carried out in the presence of the medium. The method of hai can produce; the fat of arsenic is a yellow foam. However, the aliphatic polyurethane foam contains a closed cell (cdl) in most of its structure due to the low reaction rate of the aliphatic isocyanate group, resulting in a small The cell cannot be ruptured. The closed cell structure is difficult to form on the polyurethane 6 1305540 hot press forming, so that the foam bra gasket prepared by hot press forming is a urethane containing foam. This results in slower heat dissipation efficiency and higher thermoforming temperatures and longer processing times. Residual cell membranes can only provide limited gas permeability. Another problem with thermoformed polyurethane tarpaulin gaskets It is the gas-reducing property caused by the low porosity obtained after thermoforming. Chen provides a manufacturing air hole with the upper surface and the lower surface in the 6th, 3rd, and 1st of the year 1G. The method of connecting the polyurethane 塾 塾 ,, (4) the improved permeable button, but the softness of the fresh cup made of these air holes and

外觀,帶來負面卿。絲,這鮮杯在市場上接受度極為有限。 【發明内容】 <發明之目的〉 上述習知技術的困難可由本發明加以解決。本發明可用以製作模製胸罩罩 杯’具有足分的孔隙度及透氣性。藉此製得具有抗紫外線、優異抗著色力的脂肪 族聚氨基甲酸酯發泡體胸罩罩杯。 本發明也提供-種經濟的生產胸轉㈣方法,製得具有高透氣性,並能保 持柔軟度的胸罩罩杯。 本發明的目的75在提供_種_的方法,以㈣聚氨基旨發泡材料,適 用於無接縫鮮#^、|杯、㈣及其類似物,以個在解及其他衣物。 本發明另-目的乃在提供一新穎方法,以在熱成形過程中,提昇其發泡體的 散熱,降低模製溫度及縮短製程時間。本發明的方法可防止聚合物在極高溫環境 中分解(degradation),並保護工作人員不致暴露在該熱分解所產生的有毒氫氰酸 (hydrogen cyanide)煙氣中。 本發明另-目的也在提供一模製胸罩罩杯的方法,而達到縮短製程時間的效 7 1305540 胸罩罩杯模·產_缝將得㈣顯提高 果。由於製程時間偏短, ’ 6玄胸罩罩杯包含由脂肪族 本發明另一目的也在提供一種模製胸罩杯的製程 異氰酸酯所製之熱感布及聚氨基曱酸酯發泡材料。 在業界實有需要使胸罩罩杯,終其使用期間均能維持原有顏色。所有以芳香 族異氰_所製得的聚氨基曱義發泡體皆會因照光而逐漸,並慢慢變黃而 至於呈暗棕色。通常習知技術解決這種問題的方法,即是加人—紫外線安定劑在 該聚氨基曱酸㈣泡體組成中。但該料線安定歌能延緩變黃的速度且效期Appearance, bringing negative Qing. Silk, this fresh cup is very limited in market acceptance. SUMMARY OF THE INVENTION <Objectives of the Invention> The above-described difficulties of the prior art can be solved by the present invention. The present invention can be used to make molded bra cups' having sufficient porosity and gas permeability. Thereby, an aliphatic polyurethane foam bra cup having ultraviolet resistance and excellent coloring resistance was obtained. The present invention also provides an economical production of a chest-turn (four) method for producing a bra cup having high gas permeability and maintaining softness. The object 75 of the present invention is to provide a method of using a polyamino-based foamed material, which is suitable for use in seamless joints, cups, (four) and the like, and to solve other clothes. Another object of the present invention is to provide a novel method for increasing the heat dissipation of the foam during the hot forming process, reducing the molding temperature and shortening the process time. The method of the present invention prevents degradation of the polymer in extremely high temperature environments and protects the worker from exposure to toxic hydrogen cyanide fumes produced by the thermal decomposition. Another object of the present invention is to provide a method of molding a bra cup to achieve a shorter process time. 7 1305540 Bra cover cup mold production _ seam will be (4) significantly improved. Since the process time is short, the '6 black bra cup contains a heat sensitive cloth made of an isocyanate and a polyurethane foaming material which is also a process of molding a bra cup. There is a real need in the industry for bra cups to maintain their original color during use. All of the polyamino oxime foams prepared by the aromatic isocyanine will gradually light up due to illumination and gradually turn yellow and dark brown. Conventional techniques generally solve this problem by adding an ultraviolet stabilizer to the polyaminodecanoic acid (iv) bubble composition. But the material line can stabilize the speed of yellowing and the validity period

僅及數週,在聚氨基甲_發泡體顧_發泡體最終仍會變為顯著的黃掠色。 對胸罩罩_言,以猶氰_製成的聚錄情目旨發缝實為最佳材料。 自脂肪族錄《製得的氨基曱酸㈤,化學鍵結較之料族躲曱酸乙醋不穩 定,且其化學鍵即使在低溫也可能斷裂。因此,傳統熱成形製程並不能用來模製 由脂肪族異_S旨製得之聚氨基帽轉泡體。本發明即在對習知技術提出改 進,以製造可以模㈣’由雜鋪氰_旨所製得之雜基甲義發泡體。 <發明之簡诚> 本發明提供-種聚氨基甲咖發泡體的新穎製法,製得的發泡體材料適合作 為無接_罩墊片、罩杯、罩頂及其謝讀品,_賴在鮮及其他衣物。本 發明之方法尤其適合製備_祕魏_旨與多元醇反應產生之鮮聚氨基甲 -曰發泡材料職彳代鋪無接縫鮮|杯。旨肪錢氨基^_旨發泡體係經 過網狀化k細丨MO處理,赠去财料胞_ (eeu_b麵),之後切成 片狀使其厚驗元成之解罩杯較厚部份為厚。該難無接縫鮮I杯在尖端 部或突出部具有-較厚壁,厚度較麵邊部份為厚。經過㈣之_族聚氨基甲 8 1305540 酸酯發泡體片嗣置於一母模具及一公模具組成之模具組件之間,加壓。閉合哼模 具組件並以液壓加壓。該脂肪族聚氨基甲酸酯發泡材料即因而形成與模具内腔相 同之形狀。該模製脂肪族聚氨基甲酸酯發泡材料可作為無接縫胸罩墊片、罩杯、 罩頂及類似物,供胸罩及其他衣物使用。該模製脂肪族聚氨基甲酸酯胸罩墊片具 有較習知芳香族胸罩墊片更為優異之不變黃特性,且因其提昇之透氣性及孔隙 率,而具有改善的體溫發散效果。 依據本發明一較佳實例,脂肪族聚氨基甲酸酯發泡體係在水及觸媒存在下, 直接反應脂肪族異氰義及多猶而得。經過數日之後熟化後,將聚氨基甲酸奶 發泡體團的外皮部加以切除。該聚氨基甲酸酯發泡體團另以網狀化處理 (ret—)除去發泡麟有的小胞_,得到―個實f上為僅具有骨架之網 狀結構。 在網狀化之後,將該聚氨基曱酸紐泡體切割成片,其厚度大約為所要製成 之胸罩軍杯厚度較厚部份之兩倍左右。㈣所得之聚氨基他旨發泡體片再置於 由-母觀及-公模型所組成之模具組件内,以熱。閉合該模具組件,並以 液壓施壓。施㈣聚I基曱8_發泡體㈣之壓力約為6㈣/平方忖(對模具 表面)„錄氨基甲_旨發泡材料g卩可軸與職具組制部空間綱的形狀。In only a few weeks, the polyurethane will eventually become a significant yellow smear in the polyurethane foam. For the bra cover _ words, the use of cyanide _ made by the collection of the purpose of the hair is the best material. Since the amino acid (5) obtained from the aliphatic family record, the chemical bond is unstable compared to the family of acetoacetate, and its chemical bond may be broken even at low temperatures. Therefore, the conventional thermoforming process cannot be used to mold a polyamino cap-foamed body made of an aliphatic heterogeneous. The present invention has been made in view of the prior art to produce a hetero-method foam which can be molded (four) by a cyanide. <Simplified Invention of the Invention> The present invention provides a novel method for producing a polyurethane foam, and the obtained foam material is suitable as a non-contact gasket, a cup, a cover, and a reading thereof. In fresh and other clothing. The method of the present invention is particularly suitable for the preparation of a fresh polyurethane-based foaming material produced by the reaction of a polyester with a polyol. The fat of the amino acid ^_ The foaming system is treated by reticulating k fine 丨MO, and the material is _ (eeu_b surface), and then cut into pieces to make the thickness of the cup thicker. thick. The difficult-to-join fresh I cup has a thicker wall at the tip end or the protruding portion, and the thickness is thicker than the side portion. After (4), the polyurethane 8 1305540 acid ester foam sheet is placed between a mother mold and a mold assembly composed of a male mold, and pressurized. The mold assembly is closed and pressurized with hydraulic pressure. The aliphatic polyurethane foaming material thus forms the same shape as the inner cavity of the mold. The molded aliphatic polyurethane foam can be used as a seamless bra pad, cup, hood top and the like for bras and other clothing. The molded aliphatic polyurethane bra shims have superior yellowing characteristics compared to conventional aromatic bra shims, and have improved body temperature divergence due to their improved gas permeability and porosity. According to a preferred embodiment of the present invention, the aliphatic polyurethane foaming system directly reacts with aliphatic isocyanide in the presence of water and a catalyst. After aging for several days, the outer skin portion of the polyurethane foam group was removed. The polyurethane foam group is additionally subjected to reticulation (ret-) to remove the small cells of the foaming lining, and a net-like structure having only a skeleton is obtained. After reticulation, the polyaminophthalic acid bubble is cut into a sheet having a thickness approximately twice that of the thicker portion of the bra cup to be made. (4) The obtained polyaminoethylene foam sheet is placed in a mold assembly composed of a mother-and-male model to be heated. The mold assembly is closed and pressurized with hydraulic pressure. The pressure of the (4) poly-I-based 曱8_foam (4) is about 6 (four) / square 忖 (on the surface of the mold) „ 氨基 氨基 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _

所裝仟之域聚减甲酸發鱗料即可祕無接縫鮮㈣、罩杯、罩頂 似物,供製造胸罩及直他衣物。 、 "/ΜΙ無接縫胸罩罩杯在其突出或尖端部位具有 較其週邊部份為厚之厚度。 【實施方式] 在乂下的抽3兒明中將以較佳實施例說明本發明,但應了解,在不脫離本發 明之精神及範圍之下,仍可有不同之變化騎代方案。因此該詳細僅在例示 9 1305540 本發明’作為說明之用,不得用以HP >4丨4· — <制本發明之範圍。在本發明令雖以脂肪族聚 氨基甲酸酯發泡體為例,但芳香 吳聚虱基甲馼酯發泡體仍可應用在本發明中。The field of the sputum can be used to make bras and straight clothes. , "/ΜΙSeamless bra cups have a thickness thicker than their peripheral portions at their protruding or pointed ends. [Embodiment] The present invention will be described by way of a preferred embodiment, but it should be understood that there may be variations of the alternatives without departing from the spirit and scope of the invention. Therefore, the details are only exemplified in the description of the present invention, which is used for the purpose of illustration, and may not be used in the scope of the present invention by HP >4丨4. In the present invention, an aliphatic polyurethane foam is exemplified, but an aromatic fluorenyl mercaptoester foam can be used in the present invention.

本發明是_-種聚氨齡酸㈣泡體崎難法,製得的發泡體材料適合 作為無接縫胸罩塾片、罩杯、罩頂及其類似物品,以使用在胸罩及其他衣物。本 ㈣之方法尤其適合製備簡_魏_與多元醇反應產生之軟質聚氨基甲 酸S曰發糖料職得之難無接縫胸轉杯。該脂肪族聚氨基發泡體係經 U狀化赠麵#的小胞_。其後域㈣,使其厚度較完狀胸罩罩杯 較厚部份為厚。該模健接縫胸罩罩杯在突出部或尖端部具有—較厚壁,厚度較 ”週邊。為厚。經過切片之脂肪族聚氨基甲酸g旨發泡體片嗣置於—母模具及一 公模具組紅模具歸之Fe1,域。該^祕祕。該脂肪族聚 氣基甲酸轉泡轉即_形成與·峽相同之形狀。該㈣脂職聚氨㈣ 酸嶋材料可作為無接縫胸罩墊[罩杯、罩頂及類似物,供解及其他衣物 使用。該模製脂肪族聚氨基甲酸_罩㈣具有較習知芳香族胸罩抑更為優異 之不變黃特性’且因其提昇之透氣性及孔隙率,而具有改善的體溫發散效果。 典型製作聚氨基曱酸醋發泡體的方法乃是使用下列配方,包括:⑴多元醇, ⑵水’(3)交·或鍵連增’⑷德發泡安定劑,⑴有機金屬 觸媒,(6)具有多數官能團之異氰酸醋,及⑺各種其他添加劑,例如發泡輔 助劑、填紐及防火劑。在上述成分中可使用之特定原料已為習於此藝之人士所 熟知,在此不再贅述。 在Ilia商業用聚氨基甲酸g旨發泡體時,兩種因素間互相消長抉擇,為主要的 考慮重點。這兩種因素即為膠化(gelling)及發泡(blowing)。膠化是指製造氨 10 1305540 基甲酸酯時,異氟酸酯、多元醇與交聯劑間的反應;而發泡則指異氰酸與水反應 而產生二氧化碳。如果發泡反應過速,或膠化反應過慢,則所得的發泡體會崩塌。 反之,如膨脹反應進行太慢,或膠化反應過速,則該發泡體會形成封閉的小胞結 構’其中所含的小胞會充滿因放熱反應(reaction exotherma丨)而加熱的熱氣。所 • · 製得的發泡體在冷卻、熟化後會收縮變形。 - 為生產具有良好品質及適當孔隙度之商用軟質聚氨基甲酸酯發泡體,製造過 中對膠化及發泡兩種反應的平衡,係以調整其反應組成物中胺及有機金屬觸媒 • 的含量而達成控制。孔隙或開口係以通氣量(airflow)表示。所謂之通氣量對軟 質聚氨基甲酸酯發泡體而言,是指對一 1.0吋厚之發泡體樣本上下兩面施以一標 準壓力差時,所能通過之氣流量,其單位為cfm,代表每分立方吋(cubk inchper minute)。詳細的測試方法係描述在ASTM D3574中,在本發明中引為參考。 商業用軟質聚氨基甲酸酯發泡體通常測得的通氣量為〇·5_4 〇 cfm之間。通氣 量較低之發&體有似s變形的危險,造成材料的浪費。反之,通氣量太大的發泡 體則產生嚴重的内部開裂(innerspUt) ’或甚至整個崩塌。兩者均造成製造上的 ^ 問題及材料的浪費。 發泡體内的小胞(cell)尺寸是以ppi鱗位,代表每忖孔數(p〇reper。 商用軟質聚氨基甲_旨發泡體通常具有20_100ppi的小胞尺寸^以現有的發泡設 備可以用來生產具有3-i4〇ppi小胞的聚氨基甲酸酯發泡體。 在本發明中係評估過不同小泡尺寸及孔隙度之發泡體,據以製造具有提昇透 氣性之熱成型聚氨基甲酸醋發泡體胸罩墊片。經意外發現,在熱成型胸罩塾片之 前,先將聚氣基曱酸醋發泡體網狀化,可大大提高其透氣性。雖然類似效果對各 1305540 亦即ppi值較小之發泡體而 種小胞尺寸的發泡體均可存在,但對較大小胞尺寸, 言’其提昇效果更為顯著。 本發明提供-種由脂肪族线_製造胸罩塾片之理想製程。傳統上由脂肪 族異氰酸酯製得的醋族聚氨基甲酸醋發泡體具有極封閉的結構,這是因為這種脂 肪族異氰_ 反應速麵致。所製得之難族聚氨基?義發舰通常必須 在成型後加以讎破泡使小胞膜片破裂以增加通氣量,以防止其發泡體收縮變 形。這是-種相當鋪的步驟。因為擠壓破泡需在發泡體團具有足夠強度時才能 進行。在麵之後不能立即進行麵破泡,因其時發賴_在航當中,其小 胞結構藝,如讎破齡賴其結構。且其表面妹性,也不㈣行擠壓破泡。 商業上經擠壓破泡之發泡體通常可呈現α5伽以上的通氣量,軸這種通氣量 其實不高’但已足以防止發泡體收縮變形。 經發現在聚氨基甲酸紐泡體所殘存的小胞薄膜,無論對脂肪族或芳香族者 而言,均會造成聚氨基甲酸·泡體熱成型後,發泡體孔隙度顯著降低。其理由 應不難瞭解·該殘存之小胞薄膜會―,而在該熱成型減基旨發泡體内將 含有這些細小的空氣通道,導致熱成型後的發泡體透氣性顯著下降。 本發明所製得之聚氨基甲酸醋發泡體嗣後施以網狀化加工。本發明意外的發 現’在熱步猶_狀化步驟…如本發騎示者,可以雜成型步驟中提 高該發•之賴。其結果,使紐祕料可以在較_難溫度及/或以 較短的模»賴骸熱·。這是本發明―大重鱗徵,因其可脑製程時間 並提高生產力。 有多種方法可_產生網狀化的發顏。—種方式乃是例如揭示在美國專利 12 1305540 第3,708,362號(1973年1月2日公告,頒於John J. Winchcombe等人)之網狀 化有織眼材料(例如聚氨基甲酸酯發泡體)製法。依該Winchc〇mbe發明,係將 發泡體片置於兩壓板之間’存在片狀物内封閉小胞中的氣體則以可爆氣體媒介物 ' 所代替,而引爆該媒介物,達成發泡體的網狀化。 • * 另一種網狀化聚氨基甲酸酯發泡體的方法為例如將有小胞之薄膜蝕除,其方 , 式為將發泡體浸泡在高腐錄或強酸性液體溶液t,維持-定時間。接著將發泡 體浸泡在淨水中數次。高雜性或強酸性溶液會將薄膜連同該塊體表面若干部份 φ 轉。此種方式的缺點包括:將所有腐触性/酸性殘留物自成品發泡體中移除, k為困難。此種殘留物將導致成品在網狀化數日後水解及分解。以此方法製得的 發泡體生命期有限。 另一種因降低模製溫度而得之貢獻為工作環境的改善。在習知技術之熱成型 製红中雜具套件需加熱至35〇_45昨。而施於聚氨基曱酸酯發泡體材料的壓 力則約為平方对(對模具表面),且施該聚4基曱_發泡材料之熱則約 為働F。熱及壓力需同時施加約6〇秒,實際之製程時間因該聚氨基甲酸醋發泡 φ體的厚度而異。由於習知聚氨基甲酸醋發泡材料之低導熱係數及低孔隙率,如果 為較厚之發泡體片’則需使用更長的製程時間,始能使該聚氨基甲酸醋發泡材料 、恤亦i相充分的小胞結構魏。傳統工法有—明關難,即是該聚氛基 甲酸_材料内之二縮腺(biu⑻,尿素(嶋)及氛基甲酸鍵斷裂。為處理 較厚的聚氨基甲_旨發泡材料,所需使用的較長熱成型製程時間,往往導致嚴重 題’咖是在聚氨基甲__狀材料的表_。這些化學鍵在 犯辦之下’即會發生熱分解。毒性的氫驗煙氣可嶋化學鍵斷裂而產 13 1305540 生本發明所提供的網狀化聚氨基甲酸醋發泡具有改良的散熱性 ,因而可以降低 模裝條件中所而的溫度’足以改善熱成型的效果。結果,乃得以減少毒性氮氮酸 煙氣的產生。 能降低模製溫度乙點’在脂雌聚氨基甲咖發泡體的驗型製程中極為重 —要。由脂職異級®旨製得的氨基甲_,其化學鍵強度比起芳香魏基曱酸_ * 較不穩定,因而即使在低溫仍可能分解。因此,傳統的熱成型製程無法應用在模 製由月曰肪族異氰酸製得之聚氨基甲酸醋發泡體。但因本發明所提出的改良,可以 • 传到一種模製由脂肪族異氰酸醋製得之聚氨基甲酸酯發泡體的方法。 以下的實施例說明本發明’但實施例不能代表本發明的全部。 货施例1-4 製備如表1「依本發明所製備之發泡體產物」所示之發泡體卜4。將3吋厚 10x10对長X寬之樣品捲起,並置於3升容量之壓力錯反應器中,分別進行實驗。 在每-個實驗中’壓力鋼之内部抽真空至! t〇rr,為時5分。停止抽真空並灌氧 氣進該麼力鋼’使其壓力達約250t〇rr。注入氧氣後,注入氫氣直到内壓達到大 • 約650torr。以壓力鍋内的火星裝置點燃該爆炸氣體成分。於此步驟後,檢查該 樣本。重複上述步驟,直到全部的小胞薄膜均燒除為止。每種實驗所得的發泡體 樣品命名為發泡體5至8,如表1所示。所得的發泡體5_8浸泡於蒸餾的二氣甲 烧(methylenechloride)中以除去可能因網狀化而分解的產物。發泡體樣品另以5〇 。(:之烤箱乾燥20分,冷卻,以供後續實驗之用。 依據ASTMD-3574量測該聚氨基甲酸酯發泡體之通氣量。使用的量測儀器 為Amcor (美國德州)公司產之通氣量儀,讀數以cfm為單位。另依據八81^ 14 1305540The present invention is a method for the preparation of a polyurethane-based acid (four) bubble body, which is suitable as a seamless bra enamel, cup, hood top and the like for use in bras and other clothing. The method of the above (4) is particularly suitable for preparing a soft, non-seamless chest cup of soft polyuric acid S-stained sugar produced by reacting with a polyol. The aliphatic polyamino foaming system is U-shaped to give the small cell of the surface #. The rear field (4) is thicker than the thicker portion of the finished bra cup. The molded joint bra cup has a thicker wall at the protruding portion or the tip end portion, and has a thickness smaller than the circumference. The thickness is thick. The sliced aliphatic polyurethane has a foaming sheet placed on the mother mold and a male The red mold of the mold group is classified into Fe1, the domain. The secret of the aliphatic polyglycolic acid is converted into the same shape as that of the gorge. The (4) fat polyamine (tetra) acid bismuth material can be used as a seamless joint. Bra pad [cup, cover and the like for use in solution and other clothing. The molded aliphatic polyurethane _ cover (4) has a better yellowing property than the conventional aromatic bra" and is improved The gas permeability and porosity have an improved body temperature diverging effect. The typical method for producing polyaminophthalic acid vinegar foam is to use the following formulas, including: (1) polyol, (2) water '(3) cross or bond Add '(4) defoaming stabilizer, (1) organometallic catalyst, (6) isocyanic acid vinegar with most functional groups, and (7) various other additives, such as foaming aids, fillers and fire retardants. The specific raw materials used have been used by those who have studied this art. I will not repeat them here. When Ilia commercial urethane foam is used, the two factors are mutually different, which is the main consideration. These two factors are gelling and foaming. (blowing). Gelation refers to the reaction between isoflurane, polyol and crosslinker when ammonia 10 1305540 carboxylic acid ester is produced, and foaming refers to the reaction of isocyanic acid with water to produce carbon dioxide. If the bubble reaction is too fast, or the gelation reaction is too slow, the resulting foam will collapse. Conversely, if the expansion reaction proceeds too slowly, or the gelation reaction is too fast, the foam will form a closed cell structure. The contained cells are filled with hot gas heated by the reaction exotherma. • The resulting foam shrinks and deforms after cooling and aging. - To produce commercial softness with good quality and proper porosity. Polyurethane foam, the balance between the two reactions of gelation and foaming, is controlled by adjusting the content of amine and organometallic catalyst in the reaction composition. The pores or openings are controlled by Ventilation (airf Low) indicates that the amount of ventilation refers to the soft polyurethane foam, which refers to the flow of gas that can pass when a standard pressure difference is applied to the upper and lower sides of a 1.0 吋 thick foam sample. Its unit is cfm, which stands for cubk inchper minute. Detailed test methods are described in ASTM D3574, incorporated herein by reference. Commercially available soft polyurethane foams are generally measured. The ventilation is between 〇·5_4 〇cfm. The lower ventilation volume & body has the danger of s deformation, resulting in waste of materials. Conversely, the foam with too much ventilation produces severe internal cracking (nernerspUt ) 'Or even the entire collapse. Both cause manufacturing problems and waste of materials. The size of the cell in the foam is in the ppi scale, which represents the number of pores per cell (p〇reper. Commercial soft polyurethane) foam usually has a cell size of 20-100 ppi ^ with existing foam The apparatus can be used to produce a polyurethane foam having 3-i4 〇ppi cells. In the present invention, foams having different vesicle sizes and porosity have been evaluated, and accordingly, the air permeability is improved. Thermoformed polyurethane foam bra gasket. It has been unexpectedly found that the gas-based bismuth vinegar foam is reticulated before thermoforming the bra, which greatly improves its gas permeability. For each of the 1305540, that is, the foam having a small ppi value, the small cell size foam may exist, but for the larger cell size, the effect of the improvement is more remarkable. The present invention provides a kind of aliphatic Line_The ideal process for making bra enamels. The vinegar polyurethane foams traditionally made from aliphatic isocyanates have a very closed structure because of this aliphatic isocyanide-reaction surface. The difficult family of polyamino? After the molding, the blistering is broken to break the small cell membrane to increase the ventilation to prevent the foam from shrinking and deforming. This is a relatively paved step. Because the extrusion foaming needs to have sufficient strength in the foam group. It can only be carried out. After the surface, the surface can not be broken immediately, because it is time to rely on _ in the air, its small cell structure art, such as the age of the ruined by its structure, and its surface sister, not (four) line extrusion Broken foam. Commercially extruded foamed foam can usually exhibit aeration of more than α5 gamma, and the axial ventilation is not high enough, but it is enough to prevent shrinkage and deformation of the foam. The small cell film remaining in the foam body, whether for aliphatic or aromatic, causes the porosity of the foam to be significantly reduced after the thermoformation of the polyurethane/foam body. The reason should not be difficult to understand. The small cell film will be--, and the fine air passage will be contained in the foaming body, which results in a significant decrease in gas permeability of the foam after thermoforming. Polyurethane vinegar prepared by the present invention The foam is then subjected to a reticulation process. The unexpected discovery of the invention 'in the hot step _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ The shorter model»Laiyue heat. This is the invention of the "heavy scale" because it can process the brain and increase productivity. There are many ways to produce a reticulated hair. The way is to reveal A method of reticulating a woven eye material (e.g., polyurethane foam) of U.S. Patent No. 1, 1, 305, 540, issued to Jan J. Winchcombe et al. 〇mbe invention, the foam sheet is placed between the two pressure plates 'the gas in the closed cells in the sheet is replaced by a blastable gas medium', and the medium is detonated to achieve the foam Meshing. • * Another method of reticulating polyurethane foam is to etch a film with small cells, for example, by immersing the foam in a high-corrosion or strong acid liquid solution, maintaining -set time. The foam was then immersed in clean water several times. A highly heterogeneous or strongly acidic solution will rotate the film along with portions of the surface of the block. Disadvantages of this approach include the removal of all rotched/acidic residues from the finished foam, k being difficult. This residue will cause the finished product to hydrolyze and decompose after several days of reticulation. The foam produced by this method has a limited life span. Another contribution to lowering the molding temperature is an improvement in the working environment. In the thermoforming process of the prior art, the harness set needs to be heated to 35 〇 _45 yesterday. The pressure applied to the polyurethane foam material is about square pairs (to the surface of the mold), and the heat of the poly-based foam material is about 働F. The heat and pressure need to be applied simultaneously for about 6 seconds, and the actual process time varies depending on the thickness of the polyurethane foam φ body. Due to the low thermal conductivity and low porosity of the conventional polyurethane foaming material, if it is a thick foam sheet, a longer process time is required, and the polyurethane foaming material and the shirt can be used at the beginning. The i phase is full of small cell structure Wei. The traditional method is difficult to clear, that is, the condensed gland (biu(8), urea (嶋) and the carboxylic acid bond cleavage in the poly-based formic acid _ material. For the treatment of thicker polyurethane, foaming materials, The long thermoforming process time required to use often leads to a serious problem that 'coffee is in the form of polyurethane__-like materials. These chemical bonds are under the circumstance', thermal decomposition will occur. Toxic hydrogen detection smoke The chemically cleavable bond can be produced 13 1305540. The reticulated polyurethane foam provided by the present invention has improved heat dissipation, so that the temperature in the molding conditions can be lowered to sufficiently improve the thermoforming effect. As a result, It is able to reduce the generation of toxic nitrogen oxynitride fumes. It can reduce the molding temperature. The point B is extremely heavy in the inspection process of the lipopolyamica foam. Carbamate _, its chemical bond strength is less stable than aromatic weiji decanoic acid _ *, so it may decompose even at low temperatures. Therefore, the traditional thermoforming process cannot be applied to molding from yttrium aliphatic isocyanate. Polyurethane foam. However, due to the improvement proposed by the present invention, it is possible to pass a method of molding a polyurethane foam obtained from aliphatic isocyanuric acid. The following examples illustrate the invention 'but the examples are not representative All of the present invention. Examples 1 to 4 Preparation of a foam shown in Table 1 "Foam product prepared according to the present invention" 4. A sample having a thickness of 10 x 10 and a length X width was rolled up. And placed in a 3 liter capacity of the wrong reactor, the experiment was carried out. In each experiment, 'the inside of the pressure steel was evacuated to! t〇rr, for 5 minutes. Stop vacuuming and oxygen into the force The steel has a pressure of about 250 t rr. After injecting oxygen, hydrogen is injected until the internal pressure reaches a maximum of about 650 torr. The composition of the explosive gas is ignited by the Mars device in the pressure cooker. After this step, the sample is inspected. Repeat the above steps. Until all the cell membranes were burned out. The foam samples obtained in each experiment were named as foams 5 to 8, as shown in Table 1. The obtained foams 5-8 were immersed in distilled two gas burners. (methylenechloride) to remove may be due to reticulation The product of the solution. The foam sample was further dried at 5 Torr. (: oven dried for 20 minutes, cooled for subsequent experiments. The aeration of the polyurethane foam was measured according to ASTM D-3574. The measuring instrument is an ventilator manufactured by Amcor (Texas, USA), and the reading is in cfm. The other is based on eight 81^ 14 1305540.

D-3574量測其密度,結果以為單位 ϋ矣發明所製備之發泊.體姦物 發泡體編號 ~~~-— · —-~· m" ' - in 說明 '—--- 發泡體1 旭順興業股份有限公司(臺灣嘉義)產製之芳香族聚氨基 甲酸酯發泡體;以TDIT-80及1〇〇〇當量之聚環氧丙烷二 疋醇(polypropylene 0Xide triol)製得,發泡體密度 25 kg/m3 ’小胞尺寸5〇ppi,通氣量值2 6 cfm。 ------- 發泡體2 美國密蘇里州Foamex公司所製之芳香族粗胞體聚氨基甲 酸酯發泡體,係以TDIT-80及聚醚三元醇所製成,發泡體 密度31 kg/m3 ’小胞尺寸l〇ppi,通氣量值5 2cfm。未經 網狀化。 發泡體3 旭順興業股份有限公司(臺灣嘉義)所產製之脂肪族聚氨 基甲酸酯發泡體,由異佛爾酮二異氰酸酯(is〇ph〇r〇ne diisocyanate)及聚醚多元醇反應製得,以丨.8 一二氮雜雙環 〔5.4.0〕十一婦7 (1.8-diazabicyclo (5.4.0) undecene7) 與有機金屬觸媒催化,得到發泡體密度32 kg/m3,小胞尺寸 8〇 ppi,通氣量值 0.27 cfm。 發泡體4 ( 旭順興業股份有限公司(臺灣嘉義)產製之脂肪族聚氨基 甲酸酯發泡體,由1.6己烷二異氰酸酯(1.6 hexane jiisocyanate)之預聚物與聚四甲基乙二醇鱗(p〇ly etramethylene ether glycol)反應之產物,内含18.4重量百 15 1305540 分比之游離NC〇及水—乙二醇組成物,以十酸錯㈣ 〇ct_及 u —二氮雜雙環〔5.4.0〕十—稀7(i 8 diazabiey do ( 5_4.0 ) _esene )催化,所得之發泡體密度為45 ^加3, 小胞尺寸30 ppi,通氣量值為0.12 cfm。 發泡體5 以發泡體1作網狀化處理,移除全部之小_骐,得到之 發泡物密度為23 kg/m3,通氣量值為4.9 cfm。 發泡體6 以發泡體2作網狀化處理,移除全部之小胞薄膜,得到之 發泡物密度為28 kg/m3,通氣量值為6.3 Cfm。 ~----- ' >— · 發泡體7 以發泡體3作網狀化處理,移除全部之小胞薄膜,得到之 發泡物密度為31 kg/m3,通氣量值為3,9 cfm。 .................. ,一 -- 發泡體8 以發泡體4作網狀化處理,移除全部之小胞薄膜,得到之 發泡物密度為43 kg/m3,通氣量值為6.丨cfm。 實施例5-12 將發泡體1-8置於贿之間,銘板先預熱至所需溫度,以油壓氣紅施壓。發 泡體其後即以熱成型’形成所需之厚度(發泡體9_16)。 模具套件内建電熱器’設置於-油壓震置(香港Shen_LinIndu如四公司), 該裝置可提供大_6_丨之壓力麟模魏域。絲溫歧以「κ」型熱 電偶及-數位式溫度(日本島津製作所)制並予記錄。將__片3忖厚之 發泡體片以-對!呂製壓板熱成型。壓板以内建電熱板預熱至18〇。〇,共觸秒。 兩模具元件之間距為丨叶。3G分鐘後量測所得之發泡體最終厚度,其時發泡體已 冷卻。記錄模製條件及最終發泡體厚度。 16 1305540 盘JL發泡體9-16之槿率』悴竹. 模型溫度 (最高/最低,°c) 模成型壓 力psi 成型時間 最終發泡體 厚度(吋)D-3574 measures its density, and the result is the unit made by the invention. The body lotion foam number is ~~~-- · ---~· m" ' - in description '---- foam 1 Aromatic polyurethane foam manufactured by Xushun Industrial Co., Ltd. (Chiayi, Taiwan); made with TDIT-80 and 1 〇〇〇 equivalent polypropylene 0Xide triol The foam density is 25 kg/m3 'the cell size is 5 〇ppi, and the ventilation value is 26 cfm. ------- Foam 2 Aromatic crude cell polyurethane foam made by Foamex, Missouri, USA, made of TDIT-80 and polyether triol, foaming The body density is 31 kg/m3 'the cell size l〇ppi, and the ventilation value is 5 2 cfm. Not reticulated. Foam 3 An aliphatic polyurethane foam manufactured by Xushun Industrial Co., Ltd. (Chiayi, Taiwan), consisting of isophorone diisocyanate (is〇ph〇r〇ne diisocyanate) and polyether Obtained by alcohol reaction, catalyzed by an organic metal catalyst with 丨.8-diazabicyclo[5.4.0] eleven 7 (1.8-diazabicyclo (5.4.0) undecene7) to obtain a foam density of 32 kg/m3. The small cell size is 8 〇ppi and the ventilation value is 0.27 cfm. Foam 4 (an aliphatic polyurethane foam manufactured by Xushun Industrial Co., Ltd., Taiwan Chiayi), a prepolymer of 1.6 hexane iiisocyanate and polytetramethyl b. The product of the reaction of diol scale (p〇ly etramethylene ether glycol) containing 18.4 parts by weight of 15 1305540 parts of free NC hydrazine and water-glycol composition, with octanoic acid (tetra) 〇ct_ and u-dia nitrogen Heterobicyclo[5.4.0]10-thin 7 (i 8 diazabiey do (5_4.0) _esene ) catalyzed, the obtained foam density was 45 ^ plus 3, the cell size was 30 ppi, and the aeration value was 0.12 cfm. The foam 5 was reticulated by the foam 1 to remove all the small 骐, and the obtained foam had a density of 23 kg/m 3 and aeration value of 4.9 cfm. The foam 6 was foamed. 2 for reticulation treatment, remove all the small cell membranes, the foam density is 28 kg/m3, and the aeration value is 6.3 Cfm. ~----- ' >- · Foam 7 The foam 3 is reticulated to remove all the small cell membranes, and the foam density is 31 kg/m3, and the aeration value is 3,9 cfm. ........... ......., - The foam 8 was reticulated by the foam 4, and all of the cell membranes were removed, and the foam density was 43 kg/m3, and the aeration value was 6. 丨cfm. Example 5 - 12 Put the foam 1-8 between the bribes, the nameplate is preheated to the required temperature, and pressed with oil pressure gas red. The foam is then thermoformed to form the required thickness (foam) 9_16). The mold kit built-in electric heater 'set in - oil pressure shock (Hong Kong Shen_LinIndu, such as the four companies), the device can provide a large _6_ 丨 pressure Lin model Wei domain. Silk temperature is "κ" type thermoelectric The even-and-digital temperature (Japan Shimadzu Corporation) was produced and recorded. The __ piece 3 忖 thick foam sheet was thermoformed with a pair of 吕 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压 压The total distance between the two mold elements is 丨 leaves. After 3G minutes, the final thickness of the obtained foam is measured, and the foam is cooled. The molding conditions and the final foam thickness are recorded. 16 1305540 Plate JL Foam 9-16 悴 悴 . .. Model temperature (highest / lowest, ° c) Molding pressure psi molding time final foam thickness (吋)

182/179 1+1/32 經由分析上述實驗結果可明顯看出以網狀化預處理的優異效果 實施例13-20 發泡體编號 發泡體9 發泡體10 發泡體11 發泡體12 發泡體13 發泡體14 發泡體15 發泡體16 以下列步驟量測熱成型發泡體樣本9_16之透氣性。將發泡體置於燒杯頂部, ® 觀於濕控瓶中。將整個組件存置於一溫度耽之烤箱中,以確保溫控。每隔一 小時量測該燒杯組件之質量,持續24小時。 量測水蒸氣之滲透率以顯示本發明製得之聚氨基㈣醋發泡體之透氣性。依 據刪663測試該熱成型聚氨基f酸醋發泡材料。將一氯化約乾燥劑置於玻璃燒 杯之底部’以-圓形樣板將該發泡體樣本封置至燒杯頂部,以確保發泡體表面之 區域係暴露純浦之:®度下,觀度在耽時為88·5^τ。職組件暴露於 文控制之大氣中連、.賣24小時’母隔一時間稱重,直到重量的變化趨於大致穩定。 17 1305540 當其重量變化速率成袖定後,記錄每—單位_經過雜本單位面積麥透的水 洛氣的;參透率’作為其透氣性值。 發泡體檨太夕 發泡體編號 - -…. - ---..... -:-- 達到穩定増速率 所需時間* ( h r ) 穩定時的増速率* * (g/hr) 發泡體9 4 —-- 1.46 發泡體10 3 ---~~~- ----- 2.44 發泡體11 7 ~~ ------- 0.48 發泡體12 6 _ ———-―.. 0.67 發泡體13 3 2.39 發泡體14 1 4.51 發泡體15 3 ------- 2.13 發泡體16 -------- 2 3.78 *如數個雜之料率胁5%,職驗量增加~ **增加之-定重量是依連續5次量測結果計算,得㈣平均增加量。 由上述表m可清楚_,本伽_狀域理可顯著提高熱成型聚氨基甲 酸酯發泡材料之透氣性。 本發明對於製備胸罩之墊片、軍杯 开艰似物。口,用在胸罩及其他衣 物,制翻。料❹狀方法謂品也可朗在其他有 、 產品。本發明之範圍僅得由以申Ή形狀的 暇仔㈣下丨轉種騎定義及限制。 18 1305540 【圖式簡單說明】 無圖式 【主要元件符號說明】182/179 1+1/32 By analyzing the above experimental results, the excellent effect of the reticulation pretreatment is apparent. Example 13-20 Foam No. Foam 9 Foam 10 Foam 11 Foaming Body 12 Foam 13 Foam 14 Foam 15 Foam 16 The gas permeability of the thermoformed foam sample 9_16 was measured by the following procedure. Place the foam on top of the beaker and view it in the wet bottle. Store the entire assembly in a temperature oven to ensure temperature control. The quality of the beaker assembly was measured every hour for 24 hours. The water vapor permeability was measured to show the gas permeability of the polyamino (iv) vinegar foam obtained by the present invention. The thermoformed polyamino-f vinegar foamed material was tested according to 663. Place a chlorinating approx. at the bottom of the glass beaker to seal the foam sample to the top of the beaker with a round pattern to ensure that the area of the foam surface is exposed to pure pulverization: In the case of 耽, it is 88·5^τ. The job component is exposed to the atmosphere controlled by the text, and sold for 24 hours. The weight is weighed until the change in weight tends to be substantially stable. 17 1305540 After the rate of change of weight is set, the per unit area is recorded as the permeability value of the water per unit area. Foam 檨太夕泡沫号号 - -.. - ---..... -:-- Time required to reach stable * rate* ( hr ) 増 rate at steady state * * (g/hr) Foam 9 4 --- 1.46 Foam 10 3 ---~~~- ----- 2.44 Foam 11 7 ~~ ------- 0.48 Foam 12 6 _ —— —————.. 0.67 Foam 13 3 2.39 Foam 14 1 4.51 Foam 15 3 ------- 2.13 Foam 16 -------- 2 3.78 *Several miscellaneous The material rate threat is 5%, the job amount is increased ~ ** Increased - the fixed weight is calculated based on the results of 5 consecutive measurements, and (4) the average increase. It is clear from the above table m that the gamma-like domain can significantly improve the gas permeability of the thermoformed polyurethane foam material. The invention is suitable for preparing a gasket and a military cup of a bra. Mouth, used in bras and other clothing, turned over. The method of smashing is also a product that can be used in other products. The scope of the present invention can only be defined and limited by the squatting of the scorpion (4) in the shape of the application. 18 1305540 [Simple description of the diagram] No picture [Explanation of main component symbols]

1919

Claims (1)

1305540 十、申請專利範圍: ρ·........................................ | , 4Γ2 0 年/月、曰修正+ -讎製聚氨基甲酸^旨(po丨yurethane)發泡材料的方法了包括〒~歹了夺知二丨 a) 製備—聚氨基甲酸酯發泡體; b) 將該聚氨基甲酸自旨發泡體網狀化’以實f上除去該聚氨基甲酸醋發泡 體之小胞薄膜; ' ^ c) 將该已網狀化之聚氨基甲酸酯發泡體置於預熱之模具組件間; 1 d) 施-壓力以閉合該模具組件,並形成一壓縮聚氨基甲酸醋發泡體於該[ 模具組件所形成之空間内: =1305540 X. Patent application scope: ρ·....................................... , 4 Γ 20 0 / month, 曰 correction + - 雠 聚 聚 旨 旨 旨 旨 旨 旨 旨 旨 旨 旨 旨 旨 旨 旨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 丨 制备 制备 制备 制备b) reticulating the polyurethane from the foam to remove the small cell film of the polyurethane foam; ' ^ c) the reticulated polyurethane The ester foam is placed between the preheated mold components; 1 d) applying pressure to close the mold assembly and forming a compressed polyurethane foam in the space formed by the mold assembly: ;5· e) _壓齡祕甲_旨發__絲由賴具組賴之空間所定義^ 之形狀;及 ^ f) 打開該模具組件’將該成形之聚氨基甲酸醋發泡體自該模具組件中移:丨 出。 -#· ϊ. 2.如申轉觀圍第丨賴示之方法,其巾該聚氨基㈣紐泡體包括—脂肪族錢 漆 異氰酸醋(aliphatic isocyanate)與多元醇(p〇ly〇1)在發泡劑及觸媒存在下之 反應產物。;5· e) _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ The mold assembly is moved: smashed out. -#· ϊ. 2. For example, the method of applying the guana 丨 丨 , 该 该 该 该 该 该 该 该 该 该 该 该 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚 聚1) A reaction product in the presence of a blowing agent and a catalyst. 3. 如申β專利㈣第1項所不之方法,其巾該聚氨基甲酸自旨發泡體包括—芳香族 異氰酸酯(aromatic isocyanate)與多元醇(p〇ly〇1)在發泡劑及觸媒存在下之 反應產物。 4. 如申请專利範圍第2項所示之方法,其中該脂肪族異氰酸醋為 1.6-己烷二異氰 酸醋(1‘6-hexane diisocyanate)。 5. 如申請專利範2賴*之方法’其巾旨祕異級a旨為異制酮二異氮 旨(isophorone diisocyanate) 〇 20 1305540 6. 如申請專利範圍第1項所示夕士、、t 、方法’,、中6亥聚氨基曱酸醋發泡體之厚度大於完 成後之成形聚氨基甲S_發泡體較厚部份之厚度。 ^ 7. 士申μ專舰圍第6項所不之方法’其中該聚氨基甲酸酯發泡體之厚度為完成 - 狀成形聚氨基甲酸㈣泡體較厚部份之厚度約2倍。 又‘ ·' 8.如申請專利範圍第1項所示夕古土甘士 —β 坏下之方法,其中该聚氰基甲酸酯發泡體為自一聚氨基 • 甲酸·泡體塊切割而得之聚氨基ms旨發泡體片。 9. 如申明專利副第1項所示之方法,其中該聚氨基曱酸泡體在網狀化處理 • 财該聚氨基甲酸_基質中包含實質上為網狀化之結構。 10, 如申請專利範圍第丨項所 、不之方法’另包括在將該聚氨基甲酸酯發泡體置於該 模具組件間前,在該聚氨基甲酸酿發泡體上施以一織物層之步驟。 々申β專利fc®第1項所不之方法,其巾閉合賴具組件並壓祕職基甲酸 酯發泡體之壓力係由一液壓機構所提供。 士申明專舰圍第1項所不之方法,其巾閉合賴独件並壓_聚氨基甲酸 酯發泡體之壓力對模具表面為約30_90磅/平方吋。 _ 3·Μ Μ專利In®帛1 :崎权方法’射祕騎氨基猶g旨發泡體之熱成型 時間持續约45-100秒。 14·如申請專利細第丨項所示之方法,其中該模具組件係絲熱至約a㈣〇。〔。 15·如申睛專利_第丨項所示之方法’其巾該變職氨基曱赫發泡體含有之小 胞尺寸為3-120ppi。 16 士由 ^ ‘ °申請專利範圍第15項所示之方法,其中該變形聚氨基甲義發泡體含有之 小胞尺寸為5-70ppi。 21 1305540 17·-種利用下述步驟所製得之模製聚氨基甲酸醋發泡材料··,----------- a) 製備一聚氨基甲酸酯發泡體; b) 將該錢基情·泡_狀化,上除去該聚氨基曱酸醋發泡 體之小胞薄膜; 〇將該已網狀化聚氨基甲酸醋發泡體置於預熱之模具組件間; d) 施-壓力·〗合該模具組件,並形成—壓縮聚氨基甲酸轉泡體於該 模具組件所形成之空間内; e) 將該壓縮聚氨基甲酸醋發泡體成形成為由賴具組件間之空間所定義 之形狀;及 〇打開該模具組件,將該成形之聚氨基甲酸泡體自該模具組件中移 出。 18·如申請專利範圍第17項所示之模製聚氨基甲酸醋發泡材料,其中該聚氨基甲 酸酉曰發泡體包括-脂肪族異氰酸酯(aliphaticis〇cy_e)與多元醇 在發泡劑及觸媒存在下之反應產物。 I9.如申請補I請第〗7獅枕難聚驗甲_旨發麟料,財1聚氨某甲 -日發泡體包括一方香族異氰酸I旨(ar〇matiC]jS〇Cyanate)與客- 六夕疋醇(polyol) 在發泡劑及觸媒存在下之反應產物。 2〇·如申請專職圍第18項穌之模製聚氨基甲酸自旨發泡材料,其巾娜肪於異 鼠酸Ss 為 1.6-己燒—異氰酸i旨(1.6-hexane diisocyanate )。 21·如申請翻範關18項獅之模製聚氨基甲_旨發泡材料,其中該脂肪族異 氛酸為異佛爾酮二異氰酸醋(Isophorone diisocyanate)。 22 1305540 22. 如申請專利範圍第17項所示之模製聚氨基甲酸酯發泡材料,其中該聚氨基曱 酸酿發泡體之厚度大於完成後之成形聚氨基甲酸酯發泡體較厚部份之厚度。 23. 如申請專利範圍第22項所示之模製聚氨基曱酸酯發泡材料,其中該聚氨基曱 酸醋發泡體之厚度為完成後之成形聚氨基甲酸酯發泡體較厚部份之厚度約2 倍。 24·如申請專利範圍第17項所示之模製聚氨基甲酸S旨發泡材料,其中該聚氨基甲 酸醋發泡體為自—聚氨基曱_旨發泡魏蝴而得之聚氨基曱_旨發泡體片。 25.如申轉概圍第丨7項所示之模製聚氨基曱_旨發泡㈣,其巾該聚氨基甲 酸醋發泡體在網狀化處理後在該聚氨基甲酸酯基質中包含實質上為網狀化之 結構。 26. 如申請專利範圍第17項所示之模製聚氨基甲酸醋發泡材料,另包括在將該聚 氨基甲_發泡體置於聰馳件間之前,在該聚氨基曱咖發㈣上施以一 織物層之步驟。 27. 如申請專利_ Π項所示之模製聚氨基曱義發泡材料,其中閉合該模具 組件並壓縮該聚氨基甲_旨發泡體之壓力係由—液壓機構所提供。 28. 如申請專利_ Π項所示之模製聚氨基彻旨發泡材料,其中閉合該模具 組件並壓縮該聚膽酸酿發泡體之壓力對模具表面為約购碌/平朴 .如申Μ專利範圍第17項所示之模製聚氨基 、&〜麟日發讀料,其中該壓縮聚氨 甲酉文酉曰發泡體之熱成型時間持續約45_卿秒。 申請專利範㈣Π項所故模製聚氨基甲酸§旨魏材料,其中賴具組件 係先預熱至约150-2HTC。 23 13055403. The method of the method of claim 4, wherein the polyurethane foam comprises aromatic aromatic isocyanate and polyol (p〇ly〇1) in a foaming agent and The reaction product in the presence of a catalyst. 4. The method of claim 2, wherein the aliphatic isocyanuric acid is 1.6-hexane diisocyanate. 5. As for the method of applying for the patent model 2, the method of the invention is as follows: isophorone diisocyanate 〇20 1305540 6. As shown in the first item of the patent application scope, t, method ',, the thickness of the 6-Hui polyaminophthalic acid vinegar foam is greater than the thickness of the thicker portion of the formed polyurethane S_foam after completion. ^ 7. The method of the sixth item of the Shishen μ special ship. The thickness of the polyurethane foam is about 2 times the thickness of the thicker portion of the finished shaped polyurethane. ''' 8. The method of the ancient earthenstein-β is shown in the first paragraph of the patent application scope, wherein the polycyanoformate foam is cut from a polyamino-formic acid·bubble block The obtained polyamino group is a foam sheet. 9. The method of claim 1, wherein the polyaminophthalic acid vesicle comprises a substantially reticulated structure in the reticulation treatment. 10, as in the scope of the patent application, the method of 'not including' additionally includes applying a fabric to the polyurethane foam before placing the polyurethane foam between the mold components. The steps of the layer. In the method of the patent application of the patent application, the pressure of the towel closure assembly and the pressure of the formic acid ester foam is provided by a hydraulic mechanism. The method of the first item of the special ship is not closed, and the pressure of the towel is closed and the pressure of the polyurethane foam is about 30-90 psi. _ 3·Μ Μ Patent In®帛1: The method of thermoforming of the foaming body is about 45-100 seconds. 14. The method of claim 3, wherein the mold component is hot to about a (four) 〇. [. 15. The method of the invention as claimed in the above-mentioned _ 丨 ’ 其 其 其 其 变 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱 曱The method shown in paragraph 15 of the ' ̄ ° patent application scope, wherein the modified polyurethane foam contains a cell size of 5 to 70 ppi. 21 1305540 17--Molded polyurethane foaming material prepared by the following steps, ·---------- a) Preparation of a polyurethane foam; b) the cell base is bubbled and the small cell film of the polyaminophthalic acid vinegar foam is removed; and the reticulated polyurethane foam is placed in the preheated mold assembly d) applying-pressure-combining the mold assembly and forming a compressed polyurethane foam into the space formed by the mold assembly; e) forming the compressed polyurethane foam into a Forming a shape defined by the space between the components; and opening the mold assembly to remove the formed polyurethane foam from the mold assembly. 18. The molded polyurethane foam material as disclosed in claim 17, wherein the polyurethane foam comprises - an aliphatic isocyanate (aliphaticis 〇 cy_e) and a polyol in a foaming agent and The reaction product in the presence of a catalyst. I9. If you apply for a supplement I, please refer to the 7th lion pillow to be inspected _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ And the reaction product of the guest-polyol in the presence of a blowing agent and a catalyst. 2〇·If you apply for the full-scale circumstance 18th, the molded polyurethane of the polyurethane is made of the isosuccinic acid Ss, which is 1.6-hexane diisocyanate. 21·If you apply for a model of 18 lion's molded polyurethane, the aliphatic sucrose is Isophorone diisocyanate. 22 1305540 22. The molded polyurethane foaming material according to claim 17, wherein the polyaminophthalic acid brewing foam has a thickness greater than that of the finished shaped polyurethane foam Thicker part thickness. 23. The molded polyaminophthalate foaming material as shown in claim 22, wherein the thickness of the polyaminophthalic acid vinegar foam is thicker after the formed shaped polyurethane foam The thickness of the part is about 2 times. 24. The molded polyurethane foaming material as shown in claim 17 of the patent application, wherein the polyurethane foam is a polyaminoguanidine derived from polyaminoguanidine. _The foam sheet. 25. The molded polyamino hydrazine as shown in item 7 of the application for the transfer, and the foaming of the polyurethane foam in the polyurethane matrix after the reticulation treatment. Contains a structure that is essentially meshed. 26. The molded polyurethane foaming material as shown in claim 17 of the patent application, further comprising the polyaminoglycan foam before the placing of the polyurethane foam in the box (four) The step of applying a fabric layer thereon. 27. The molded polyamino oxime foaming material as disclosed in the patent application, wherein the pressure of closing the mold assembly and compressing the polyurethane foam is provided by a hydraulic mechanism. 28. The molded polyamino resin foaming material as disclosed in the patent application, wherein the pressure of the mold component is closed to the mold surface by closing the mold assembly and compressing the pressure of the polycholesteric foam. The molded polyamino group, &~Lin Rifa reading material shown in Item 17 of the patent application scope, wherein the compression molding time of the compressed polyurethane foam is about 45 _ sec. Patent application (4) applies for the molding of polyurethane § wei materials, in which the components are preheated to about 150-2HTC. 23 1305540 Φ 31. 如申請專利範圍第17項所示之模製聚氨基曱酸酯發泡材料, 基曱酸酯發泡體含有之小胞尺寸為3-120ppi。 32. 如申請專利範圍第31項所示之模製聚氨基甲酸酯發泡材料, 基曱酸酯發泡體含有之小胞尺寸為5-70 ppi。 33. 如申請專利範圍第31項所示之模製聚氨基甲酸酯發泡材料, 基甲酸酯發泡體含有之小胞尺寸為3-40ppi。 34. 如申請專利範圍第33項所示之模製聚氨基曱酸酯發泡材料, 基甲酸酯發泡體為胸罩墊片。 其中該變形聚氨 其中該變形聚氨 其中該變形聚氨 其中該變形聚氨Φ 31. The molded urethane foam material as shown in claim 17 of the patent application, the bismuth phthalate foam contains a small cell size of 3-120 ppi. 32. The molded urethane foam material according to claim 31, wherein the bismuth phthalate foam contains a cell size of 5 to 70 ppi. 33. The molded polyurethane foam according to claim 31, wherein the urethane foam contains a cell size of 3 to 40 ppi. 34. The molded urethane foaming material according to claim 33, wherein the urethane foam is a bra shim. Wherein the deformed polyamine, wherein the deformed polyamine, wherein the deformed polyamine, the deformed polyamine 24twenty four
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