JPH0519599B2 - - Google Patents
Info
- Publication number
- JPH0519599B2 JPH0519599B2 JP12440285A JP12440285A JPH0519599B2 JP H0519599 B2 JPH0519599 B2 JP H0519599B2 JP 12440285 A JP12440285 A JP 12440285A JP 12440285 A JP12440285 A JP 12440285A JP H0519599 B2 JPH0519599 B2 JP H0519599B2
- Authority
- JP
- Japan
- Prior art keywords
- parts
- petroleum gas
- liquefied
- liquefied petroleum
- gas
- 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.)
- Expired - Lifetime
Links
- 239000003915 liquefied petroleum gas Substances 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 22
- 239000007789 gas Substances 0.000 claims description 20
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 16
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 13
- 239000001273 butane Substances 0.000 claims description 11
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 11
- 239000002904 solvent Substances 0.000 claims description 11
- 239000012046 mixed solvent Substances 0.000 claims description 8
- 239000001294 propane Substances 0.000 claims description 8
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- 239000004435 Oxo alcohol Substances 0.000 claims description 6
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000011347 resin Substances 0.000 claims description 6
- 229920005989 resin Polymers 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 6
- JSPLKZUTYZBBKA-UHFFFAOYSA-N trioxidane Chemical compound OOO JSPLKZUTYZBBKA-UHFFFAOYSA-N 0.000 claims description 5
- ALSTYHKOOCGGFT-KTKRTIGZSA-N (9Z)-octadecen-1-ol Chemical compound CCCCCCCC\C=C/CCCCCCCCO ALSTYHKOOCGGFT-KTKRTIGZSA-N 0.000 claims description 4
- 239000005062 Polybutadiene Substances 0.000 claims description 4
- 229940055577 oleyl alcohol Drugs 0.000 claims description 4
- XMLQWXUVTXCDDL-UHFFFAOYSA-N oleyl alcohol Natural products CCCCCCC=CCCCCCCCCCCO XMLQWXUVTXCDDL-UHFFFAOYSA-N 0.000 claims description 4
- 229920002857 polybutadiene Polymers 0.000 claims description 4
- 239000000010 aprotic solvent Substances 0.000 claims description 3
- 150000002148 esters Chemical class 0.000 claims description 2
- 229920003049 isoprene rubber Polymers 0.000 claims description 2
- JTXAHXNXKFGXIT-UHFFFAOYSA-N propane;prop-1-ene Chemical group CCC.CC=C JTXAHXNXKFGXIT-UHFFFAOYSA-N 0.000 claims description 2
- FMZUHGYZWYNSOA-VVBFYGJXSA-N (1r)-1-[(4r,4ar,8as)-2,6-diphenyl-4,4a,8,8a-tetrahydro-[1,3]dioxino[5,4-d][1,3]dioxin-4-yl]ethane-1,2-diol Chemical compound C([C@@H]1OC(O[C@@H]([C@@H]1O1)[C@H](O)CO)C=2C=CC=CC=2)OC1C1=CC=CC=C1 FMZUHGYZWYNSOA-VVBFYGJXSA-N 0.000 description 11
- 229940087101 dibenzylidene sorbitol Drugs 0.000 description 11
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 9
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 8
- 229960002920 sorbitol Drugs 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 6
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 6
- 238000011049 filling Methods 0.000 description 6
- 239000000446 fuel Substances 0.000 description 6
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000000600 sorbitol Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- ZNQVEEAIQZEUHB-UHFFFAOYSA-N 2-ethoxyethanol Chemical compound CCOCCO ZNQVEEAIQZEUHB-UHFFFAOYSA-N 0.000 description 4
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000499 gel Substances 0.000 description 3
- 239000003349 gelling agent Substances 0.000 description 3
- 239000001282 iso-butane Substances 0.000 description 3
- 239000002798 polar solvent Substances 0.000 description 3
- 239000003377 acid catalyst Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- OHLUUHNLEMFGTQ-UHFFFAOYSA-N N-methylacetamide Chemical compound CNC(C)=O OHLUUHNLEMFGTQ-UHFFFAOYSA-N 0.000 description 1
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 1
- 235000011613 Pinus brutia Nutrition 0.000 description 1
- 241000018646 Pinus brutia Species 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 235000010985 glycerol esters of wood rosin Nutrition 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 150000003138 primary alcohols Chemical class 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- -1 unsaturated aliphatic alcohols Chemical class 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は取扱いが容易でしかもその蒸発が液体
状態の場合に比してゆるやかな固型化された液化
石油ガス組成物に関し、例えばガスライターの燃
料の固型化された組成物に関する。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a solidified liquefied petroleum gas composition that is easy to handle and evaporates more slowly than in a liquid state. The present invention relates to a solidified composition of fuel.
(従来の技術)
従来ガスライターの燃料としてはプロパン、ブ
タン等の常温常圧下ではガス状の燃料が使用され
ているが、これらは何れも密閉容器中では自己の
蒸気圧によつて加圧されて液体となつており使用
時容器を開放すると気化して燃料として供される
のである。しかして往々にして容器の破損等によ
り開放された状態になつた場合、瞬時に気化して
大量のものがガスとなり、また充填時も細心の注
意が必要である。特に充填に際しては例えば冷却
充填方式によれば液化ブタンガスは気化しやすい
ために−50〜−60℃に冷却して行なわねばなら
ず、そのため常温使用時におけるガス量のバラツ
キが生じやすい等の欠点があつた。(Prior art) Conventional gas lighters use propane, butane, and other fuels that are gaseous at room temperature and pressure, but these are all pressurized by their own vapor pressure in a closed container. When the container is opened, it vaporizes and is used as fuel. However, if the container is opened due to breakage or the like, it will instantly vaporize and a large amount will become gas, and great care must be taken when filling. In particular, when filling, for example, if the cooling filling method is used, liquefied butane gas easily vaporizes, so it must be cooled to -50 to -60°C, which has disadvantages such as the tendency to vary the amount of gas when used at room temperature. It was hot.
(発明が解決すべき問題点)
本発明者らは上記のような取扱い困難な液化石
油ガスを固型化し、取扱いを容易にするため種々
検討を行つた結果本発明を完成するに至つもたの
で、本発明の目的は取扱い容易な固型化された液
化石油ガス組成物に関する。(Problems to be Solved by the Invention) The present inventors have completed the present invention as a result of various studies in order to solidify the liquefied petroleum gas, which is difficult to handle, and make it easier to handle. Therefore, an object of the present invention is to provide a solidified liquefied petroleum gas composition that is easy to handle.
(問題点を解決するための手段)
すなわち本発明は液化石油ガスと固形剤及び液
化ガスと相溶性を有する溶媒と非プロトン系溶媒
とからなる混合溶媒に少量のレジンを添化して得
られた固型化された液化石油ガス組成物であつ
て、本発明における液化石油ガスとは常温常圧下
ではガス状を呈する石油系又は天然ガス系炭化水
素を圧縮又は同時に冷却して液状としたもので主
としてプロパンまたはブタンであるが、燃料とし
て使用される液化ブタン(ブタン−ブチレン混合
物)及び液化プロパン(プロパン−プロピレン混
合物)をも云う。これらの液状のガスを固形化す
る固形剤すなわちゲル化剤としてはジベンジリデ
ンソルビトール又はトリベンジリデンソルビトー
ル又はこれらの核置換誘導体が使用できるがジベ
ンジリデンソルビトールとトリベンジリデンソル
ビトールとの混合物が最も好ましい。しかしてこ
れらのソルビトール化合物はDソルビトールにベ
ンズアルデヒド又はその核置換体を酸触媒の存在
で脱水縮合させて得た白色粉末であつて、これら
はジメチルホルムアミド又はN−メチル・2・ピ
ロリドンのような非プロトン系の溶媒に高濃度で
溶解する。(Means for Solving the Problems) That is, the present invention is obtained by adding a small amount of resin to a mixed solvent consisting of liquefied petroleum gas, a solid agent, a solvent compatible with the liquefied gas, and an aprotic solvent. It is a solidified liquefied petroleum gas composition, and the liquefied petroleum gas in the present invention is a petroleum-based or natural gas-based hydrocarbon that is gaseous at normal temperature and pressure, and is made into a liquid by compressing or simultaneously cooling it. Primarily propane or butane, but also liquefied butane (butane-butylene mixture) and liquefied propane (propane-propylene mixture) used as fuel. As the solid agent or gelling agent for solidifying these liquid gases, dibenzylidene sorbitol, tribenzylidene sorbitol, or nuclear substituted derivatives thereof can be used, but a mixture of dibenzylidene sorbitol and tribenzylidene sorbitol is most preferred. These sorbitol compounds are white powders obtained by dehydrating and condensing benzaldehyde or its nuclear substituted product with D-sorbitol in the presence of an acid catalyst, and these are white powders obtained by dehydrating and condensing D-sorbitol with benzaldehyde or its nuclear substituted product in the presence of an acid catalyst. Dissolves in proton-based solvents at high concentrations.
ところで液化石油ガスを固型化するに当つて
は、ゲル化剤を非プロトン系溶媒に溶解し、この
溶液を液化石油ガスに混合することが考えられる
が、固型化される液化石油ガスは非極性であるた
め非プロトン系極性溶媒である、ジメチルホルム
アミドやN−メチル・2・ピロリドンと全く相溶
性を有しないのでこの方法では固型化することが
できない。また、プロパン、ブタン等と相溶する
溶媒にジベンジリデンソルビトールのようなゲル
化剤を入れるとゲル化を生じ溶液とすることがで
きない。この点を改良する為に種々の研究を行つ
た結果、プロパン、N−ブタン、イソブタン等に
相溶性がある特定の溶媒と非プロトン系極性溶媒
であるジメチルアセトアミド又はN−メチル・
2・ピロリドン又はその混合物との混合溶媒にジ
ベンジリデンソルビトール又はトリベンジリデン
ソルビトール等を溶解しこれに液化石油ガスを添
加して液化石油ガスを固型化することを見出し
た。すなわち、この溶媒としてはアセトン、オキ
ソ法によつて得られた炭素数8ないし18個で代表
される直鎖状1級アルコール(以下オキソアルコ
ールという)又はオレイルアルコールの如き不飽
和脂肪族アルコールをあげることができる。この
混合溶剤における液化石油ガスと相溶性のある溶
媒と非プロトン系極性溶媒との混合比は各溶媒の
組合せによつて種々変更できるが例えばジメチル
アセトアミドとオキソアルコールとの場合では前
者が75部〜65部(重量)、後者が25部〜35部(重
量)の間が最も好ましく、ジメチルアセトアミド
が75重量部以上では固化される液化石油ガスとの
相溶性が悪く、65重量部より少ないと固形化剤例
えばジベンジリデンソルビトールを溶解しても溶
液となることなく固形化剤自体がゲル化し使用が
不能となる。また混合溶剤にエチルセルソルブを
添加することにより冷却した場合に固形化剤の溶
液が急激にゲル化を生ずるのを防ぐ作用があり、
通常1〜5部の間の任意の量を使用することがで
きる。 By the way, when solidifying liquefied petroleum gas, it is possible to dissolve the gelling agent in an aprotic solvent and mix this solution with liquefied petroleum gas, but the liquefied petroleum gas to be solidified is Since it is nonpolar, it has no compatibility with dimethylformamide or N-methyl-2-pyrrolidone, which are aprotic polar solvents, and therefore cannot be solidified by this method. Furthermore, if a gelling agent such as dibenzylidene sorbitol is added to a solvent that is compatible with propane, butane, etc., gelation occurs and it is impossible to form a solution. As a result of conducting various studies to improve this point, we found that a specific solvent that is compatible with propane, N-butane, isobutane, etc. and dimethylacetamide or N-methylacetamide, which is an aprotic polar solvent, were used.
It has been discovered that dibenzylidene sorbitol or tribenzylidene sorbitol, etc. is dissolved in a mixed solvent with 2.pyrrolidone or a mixture thereof, and liquefied petroleum gas is added thereto to solidify the liquefied petroleum gas. That is, examples of the solvent include acetone, linear primary alcohols having 8 to 18 carbon atoms obtained by the oxo method (hereinafter referred to as oxo alcohols), and unsaturated aliphatic alcohols such as oleyl alcohol. be able to. The mixing ratio of the solvent compatible with liquefied petroleum gas and the aprotic polar solvent in this mixed solvent can be varied depending on the combination of each solvent, but for example, in the case of dimethylacetamide and oxo alcohol, the former is 75 parts to 65 parts (by weight), and the latter is most preferably between 25 and 35 parts (by weight). If dimethylacetamide exceeds 75 parts by weight, it will have poor compatibility with the liquefied petroleum gas to be solidified, and if it is less than 65 parts by weight, it will become solid. Even if a solidifying agent such as dibenzylidene sorbitol is dissolved, it does not become a solution and the solidifying agent itself gels, making it impossible to use. In addition, adding ethyl cellosolve to the mixed solvent has the effect of preventing the solidifying agent solution from rapidly gelling when cooled.
Any amount typically between 1 and 5 parts can be used.
なおガスライターの燃料に当つてはライターの
炎に煤を発生しないことが大切であり、その為に
芳香族系の溶媒は使用することができない。ま
た、一般にガスライターの容器はプラスチツクの
容器が使用されているため、プラスチツクを溶解
しない溶媒が良いと思われるが上記の溶媒の中で
はオキソアルコール、オレイルアルコールが最も
好ましい。 When it comes to fuel for gas lighters, it is important that the lighter's flame does not generate soot, and for this reason aromatic solvents cannot be used. Furthermore, since plastic containers are generally used for gas lighter containers, it is thought that a solvent that does not dissolve plastic is preferable, but among the above-mentioned solvents, oxo alcohol and oleyl alcohol are most preferred.
ジベンジリデンソルビトール又はトリベンジリ
デンソルビトールの溶解量は混合溶剤100重量部
に対して3部から25部の範囲であつて、好ましく
は5重量部から20重量部である。3部以下では得
られる固型化液化ガスの強度が弱く25部以上にな
ると冷却したとき混合溶剤がゲル化を生ずる。ま
た、ジベンジリデンソルビトール又はトリベンジ
リデンソルビトール等の所要量は固型化される組
成物100重量部中0.5重量部から4重量部であり、
0.5重量部以下では得られる液化ガスの固型化物
が弱くて軟かいジエリー状となり4重量部以上で
は析出して白化を起す。 The amount of dibenzylidene sorbitol or tribenzylidene sorbitol dissolved is in the range of 3 to 25 parts, preferably 5 to 20 parts by weight, per 100 parts by weight of the mixed solvent. If it is less than 3 parts, the strength of the solidified liquefied gas obtained will be weak, and if it is more than 25 parts, the mixed solvent will gel when cooled. Further, the required amount of dibenzylidene sorbitol or tribenzylidene sorbitol is from 0.5 parts by weight to 4 parts by weight based on 100 parts by weight of the composition to be solidified.
If it is less than 0.5 parts by weight, the solidified product of the liquefied gas obtained will be weak and soft in the form of jewelery, and if it is more than 4 parts by weight, it will precipitate and cause whitening.
次に固型化物の強度を増す為に少量のレジンを
添加する必要があるが固型化される液化ガスに溶
解するレジン類は極めて少なく、ロジン、エステ
ルガス、ロジン誘導体、イソプレンゴム、ポリブ
タジエン等が使用され、その添加量は固形化され
る液化石油ガス100部(重量)に対し0.01部〜15
部、好ましくは0.1部〜5部(重量)、更に好まし
くは0.2部〜2部であつて0.01部より少ない場合
には軟かすぎて成形しにくゝ、15部以上では溶解
が困難となり白濁を生ずる。 Next, it is necessary to add a small amount of resin to increase the strength of the solidified product, but there are very few resins that dissolve in the liquefied gas that is solidified, such as rosin, ester gas, rosin derivatives, isoprene rubber, polybutadiene, etc. is used, and the amount added is 0.01 to 15 parts per 100 parts (weight) of liquefied petroleum gas to be solidified.
parts, preferably 0.1 parts to 5 parts (by weight), more preferably 0.2 parts to 2 parts; if it is less than 0.01 parts, it will be too soft and difficult to mold, and if it is more than 15 parts, it will be difficult to dissolve and it will become cloudy. will occur.
次に実施例を挙げて本発明を説明する。なお以
下の数字は何れも重量である。 Next, the present invention will be explained with reference to Examples. All numbers below are weights.
実施例 1
ブタンガスを−10℃に冷却して液化し、これの
95.5部に対してロジン0.5部を加え撹拌して溶解
する。別にジメチルアセトアミド65部、オキソア
ルコール25部とからなる混合溶剤を作り、この中
にジベンジリデンソルビトール9部を加え80℃に
加熱して完全に溶解させ、更にエチルセルソルブ
1部を添加する。この溶液は−10℃迄冷却しても
直ぐにはゲル化することなく溶液状態で存在し得
る。次に先に得られたロジンを混合したブタン90
部にジベンジリデンソルビトールを溶解したジメ
チルアセトアミド、オキソアルコール及びエチル
セルソルブの混合溶液10部を混合するとゲルを生
じ稍固い固体状の液化ガスを得る。これを任意の
形に切断し容器に封入することが可能である。な
お、上記の操作はすべて−10℃で行いブタンの気
化を極力防止することは必要であるが固型化され
たブタンガスは極めて安定であつてそのまゝ放置
しておくと徐々に気化して小さい塊となり非常に
ゆるやかに蒸発して行くことがわかる。Example 1 Butane gas is cooled to -10℃ and liquefied.
Add 0.5 part of rosin to 95.5 parts and stir to dissolve. Separately, prepare a mixed solvent consisting of 65 parts of dimethylacetamide and 25 parts of oxo alcohol, add 9 parts of dibenzylidene sorbitol to it, heat it to 80°C to completely dissolve it, and then add 1 part of ethyl cellosolve. This solution can exist in a solution state without immediately gelling even when cooled to -10°C. Next, butane 90 mixed with the rosin obtained earlier
When mixed with 10 parts of a mixed solution of dimethylacetamide, oxo alcohol and ethyl cellosolve in which dibenzylidene sorbitol is dissolved, a gel is formed and a slightly hard solid liquefied gas is obtained. It is possible to cut this into any shape and seal it in a container. Although it is necessary to perform all of the above operations at -10℃ to prevent the vaporization of butane as much as possible, solidified butane gas is extremely stable and will gradually vaporize if left as is. It can be seen that it forms small lumps and evaporates very slowly.
実施例 2
実施例1におけるブタンガスの代りにプロパン
ガスを使用し、−45℃のもとでポリブタジエンを
溶解して次の1液を作る。Example 2 Using propane gas instead of butane gas in Example 1, polybutadiene was dissolved at -45°C to prepare the following liquid.
1液 液化プロパン 95.5部
ポリブタジエン 0.5部
同様に下記の組成を混合して80℃に加温して溶
解し2液をつくる。 1st liquid: 95.5 parts of liquefied propane, 0.5 parts of polybutadiene. Similarly, mix the following composition and heat to 80°C to dissolve and make 2nd liquid.
2液 トリベンジリデンソルビトール 3部
ジベンジリデンソルビトール 2部
N・メチル・2・ピロリドン 80部
アセトン 13部
2液を−45℃に冷却し−45℃にある1液を混合
すると直ちに固型化して固い寒天状のものを得
る。 2 parts Tribenzylidene sorbitol 3 parts Dibenzylidene sorbitol 2 parts N-methyl-2-pyrrolidone 80 parts Acetone 13 parts When the 2 parts are cooled to -45°C and the 1 part at -45°C is mixed, it immediately solidifies and becomes hard agar. get something like that.
実施例 3
実施例1と同様にして−20℃で次の1液をつく
る。Example 3 In the same manner as in Example 1, prepare the following solution at -20°C.
1液 液化イソブタン 99部
エステルガム 0.5部
松 脂 0.5部
同様にして次の組成のものを混合し80℃加温し
て完全に溶解し2液をつくる。 Part 1: Liquefied isobutane 99 parts Ester gum 0.5 parts Pine resin 0.5 parts In the same manner, mix the following compositions and heat to 80℃ to completely dissolve and make Part 2.
2液 ジベンジリデンソルビトール 10部
N・メチル・2・ピロリドン 50部
ジメチルアセトアミド 18部
オレイルアルコール 20部
エチルセルソルブ 2部
次に1液と2液とを−20℃で混合すると直ちに
固型化を生じ固状のイソブタン組成物を得る。 Part 2 Dibenzylidene sorbitol 10 parts N-methyl-2-pyrrolidone 50 parts Dimethylacetamide 18 parts Oleyl alcohol 20 parts Ethyl cellosolve 2 parts Next, when parts 1 and 2 are mixed at -20°C, solidification occurs immediately. A solid isobutane composition is obtained.
(効果)
本発明の固型化された液化石油ガス組成物は極
めて安定で且つ取扱いも容易であり、しかも所望
の形状に成形することも可能となり特にガスライ
ター用の燃料を固型化することによつて従来のよ
うな−50℃〜−60℃に冷却して充填する冷却充填
方式や窒素ガス等による強制的に加圧して充填す
る加圧充填方式をを採用することなく、極めて容
易に充填することができる等の効果を奏するもの
である。(Effects) The solidified liquefied petroleum gas composition of the present invention is extremely stable and easy to handle, and can also be molded into a desired shape, particularly for solidifying fuel for gas lighters. This eliminates the need for the conventional cooling filling method in which the product is cooled to -50°C to -60°C before filling, or the pressurized filling method in which the product is forcibly pressurized using nitrogen gas or the like. This has effects such as being able to be filled.
Claims (1)
を有する溶媒と非プロトン系溶媒とからなる混合
溶媒に少量のレジンを添加して得られる固型化さ
れた液化石油ガス組成物。 2 液化石油ガスが液化プロパン(プロパン・プ
ロピレン混合物)又は液化ブタン(ブタン−ブチ
レン混合物)である特許請求の範囲第1項記載の
固型化された液化石油ガス組成物。 3 液化石油ガスと相溶性を有する溶媒としてア
セトン、オキソアルコール及びオレイルアルコー
ルからなる群から選ばれたものである特許請求の
範囲第1項記載の固型化された液化石油ガス組成
物。 4 レジンがロジン、エステルガス、ロジン誘導
体、イソプレンゴム及びポリブタジエンからなる
群から選ばれたものである特許請求の範囲第1項
記載の固型化された液化石油ガス組成物。[Claims] 1. Solidified liquefied petroleum gas obtained by adding a small amount of resin to a mixed solvent consisting of liquefied gas, a solid agent, a solvent compatible with liquefied petroleum gas, and an aprotic solvent. Composition. 2. The solidified liquefied petroleum gas composition according to claim 1, wherein the liquefied petroleum gas is liquefied propane (propane-propylene mixture) or liquefied butane (butane-butylene mixture). 3. The solidified liquefied petroleum gas composition according to claim 1, wherein the solvent that is compatible with liquefied petroleum gas is selected from the group consisting of acetone, oxo alcohol, and oleyl alcohol. 4. The solidified liquefied petroleum gas composition according to claim 1, wherein the resin is selected from the group consisting of rosin, ester gas, rosin derivatives, isoprene rubber, and polybutadiene.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12440285A JPS61283693A (en) | 1985-06-10 | 1985-06-10 | Consolidated liquefied petroleum gas composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12440285A JPS61283693A (en) | 1985-06-10 | 1985-06-10 | Consolidated liquefied petroleum gas composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61283693A JPS61283693A (en) | 1986-12-13 |
| JPH0519599B2 true JPH0519599B2 (en) | 1993-03-17 |
Family
ID=14884557
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12440285A Granted JPS61283693A (en) | 1985-06-10 | 1985-06-10 | Consolidated liquefied petroleum gas composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61283693A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01184330A (en) * | 1988-01-14 | 1989-07-24 | Iwatsukusu:Kk | Gas lighter |
| JPH01129536U (en) * | 1988-02-19 | 1989-09-04 | ||
| JPH0236735U (en) * | 1988-08-30 | 1990-03-09 | ||
| CN101955827B (en) * | 2010-09-07 | 2013-02-13 | 山东三维石化工程股份有限公司 | Preparation method of solid natural gas hydrate |
-
1985
- 1985-06-10 JP JP12440285A patent/JPS61283693A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61283693A (en) | 1986-12-13 |
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