- InChI
- InChI=1S/C6H12Cl2O/c1-5(3-7)9-6(2)4-8/h5-6H,3-4H2,1-2H3
- InChI Key
- QCFYJCYNJLBDRT-UHFFFAOYSA-N
- Formula
- C6H12Cl2O
- SMILES
- CC(CCl)OC(C)CCl
- Molecular Weight1
- 171.07
- CAS
- 108-60-1
- Other Names
-
- (2-Chloro-1-methylethyl) ether
- 2,2'-Dichlorodiisopropyl ether
- 2,2'-Dichloroisopropyl ether
- BIS(2-CHLORO-1-METHYLETHYL) ETHER
- Bis(1-chloro-2-propyl) ether
- Bis(«beta»-chloroisopropyl) ether
- DCIP
- DCIP (Nematocide)
- Dichlorodiisopropyl ether
- Dichloroisopropyl ether
- Ether, bis(2-chloro-1-methylethyl)
- NCI-C50044
- NSC 2849
- «beta»,«beta»'-Dichlorodiisopropyl ether
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4056 | Relay (1.0) Calculated Property | |
| ΔfG° | -134.10 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -384.71 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 13.83 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.86 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.95 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.52 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.258 | Crippen Calculated Property | |
| McVol | 125.750 | ml/mol | McGowan Calculated Property |
| Pc | 2862.74 | kPa | Joback Calculated Property |
| Inp | [171.60; 1029.00] |
|
|
| Inp | 171.60 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 171.60 | NIST | |
| Ip | 1464.00 | NIST | |
| Tboil | [460.20; 460.25] | K |
|
| Tboil | 460.20 | K | NIST |
| Tboil | 460.25 | K | NIST |
| Tc | 630.80 | K | Relay (1.0) Calculated Property |
| Tfus | 176.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.447 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 53.60 | kJ/mol | 379.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [174.35; 364.99] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.53520e+01 | |||
| Coefficient B | 5.36040e-01 | |||
| Coefficient C | -2.38800e-04 | |||
| Coefficient D | 2.24000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 174.35 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 206.09 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 235.03 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 261.24 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 284.78 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 305.73 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 324.15 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 340.12 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 353.71 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 364.99 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0302383; 0.0002531] | Pa×s | [176.15; 435.05] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.15359e+01 | |||
| Coefficient B | 1.41577e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 176.15 | |||
| Temperature range, max. | 435.05 | |||
| η | 0.0302383 | Pa×s | 176.15 | Calculated Property |
| η | 0.0097848 | Pa×s | 204.92 | Calculated Property |
| η | 0.0041801 | Pa×s | 233.68 | Calculated Property |
| η | 0.0021517 | Pa×s | 262.45 | Calculated Property |
| η | 0.0012629 | Pa×s | 291.21 | Calculated Property |
| η | 0.0008158 | Pa×s | 319.98 | Calculated Property |
| η | 0.0005663 | Pa×s | 348.75 | Calculated Property |
| η | 0.0004156 | Pa×s | 377.51 | Calculated Property |
| η | 0.0003187 | Pa×s | 406.28 | Calculated Property |
| η | 0.0002531 | Pa×s | 435.05 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [344.12; 563.57] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.19304e+01 | |||
| Coefficient B | -3.36626e+03 | |||
| Coefficient C | -5.49930e+01 | |||
| Temperature range, min. | 344.12 | |||
| Temperature range, max. | 563.57 | |||
| Pvap | 1.33 | kPa | 344.12 | Calculated Property |
| Pvap | 3.30 | kPa | 368.50 | Calculated Property |
| Pvap | 7.16 | kPa | 392.89 | Calculated Property |
| Pvap | 13.99 | kPa | 417.27 | Calculated Property |
| Pvap | 25.14 | kPa | 441.65 | Calculated Property |
| Pvap | 42.14 | kPa | 466.04 | Calculated Property |
| Pvap | 66.65 | kPa | 490.42 | Calculated Property |
| Pvap | 100.43 | kPa | 514.80 | Calculated Property |
| Pvap | 145.20 | kPa | 539.19 | Calculated Property |
| Pvap | 202.65 | kPa | 563.57 | Calculated Property |
| Pvap | [0.13; 102.37] | kPa | [302.80; 455.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.61227e+01 | |||
| Coefficient B | -4.80618e+03 | |||
| Coefficient C | -3.77570e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 302.80 | |||
| Temperature range, max. | 455.90 | |||
| Pvap | 0.13 | kPa | 302.80 | Calculated Property |
| Pvap | 0.40 | kPa | 319.81 | Calculated Property |
| Pvap | 1.05 | kPa | 336.82 | Calculated Property |
| Pvap | 2.50 | kPa | 353.83 | Calculated Property |
| Pvap | 5.44 | kPa | 370.84 | Calculated Property |
| Pvap | 10.96 | kPa | 387.86 | Calculated Property |
| Pvap | 20.71 | kPa | 404.87 | Calculated Property |
| Pvap | 36.98 | kPa | 421.88 | Calculated Property |
| Pvap | 62.87 | kPa | 438.89 | Calculated Property |
| Pvap | 102.37 | kPa | 455.90 | Calculated Property |
Similar Compounds
![Isopropyl [2-chloro-1-(chloromethyl)ethyl] ether.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAYLUlEQVR4nO3de1QTVx4H8F8ggYSXIq6gYB+IYMHWRVoRWOvW46tdEFARtW7XWsU9K+LpqfWxro2ednuwe6xUq1utVlFbNdYqKMIqCiyCq5tYxYCAvKyCojwTJIQ87v4xLCoF5DHJTLi/z/EPJZN7f+CXydxfZiYCQgggRAcrrgtAyHww7ogiGHdEEYw7ogjGHVEE444ognFHFMG4I4pg3BFFMO6IIhh3RBGMO6IIxh1RBOOOKIJxRxTBuCOKYNwRRTDuiCIYd0QRjDuiCMYdUQTjjiiCcUcUwbgjimDcEUUw7ogiGHdEEYw7ogjGHVEE444ognFHFMG4I4pg3BFFMO6IIhh3RBGMO6IIxh1RBOOOKIJxRxTBuCOKYNwRRTDuiCIYd0QRjDuiCMYdUQTjjiiCcUcUwbgjimDcEUUw7ogiGHdEEYw7ogjGHVEE444ognFHFMG4I4pg3BFFMO6IIhh3RBGMO6IIxh1RBOOOKIJxRxTBuCOKYNwRRTDuiCIYd0QRjDuiCMYdUQTjjiiCcUcUwbgjimDcEUUw7ogiGHdEEYw7ogjGHVGkR3HX6XSlpaWmLgUhU+tR3FeuXOnv73/mzBlTV4OQST0/7jqdrqamRq1WR0ZGfv3112aoCSETeX7cRSLR8ePH4+PjDQbDypUrY2JidDqdGSpDiHUCQkgPN5XJZIsXL9ZoNJMmTTpx4sRvfvMbk1aGEOt6EXcAuHLlSkRExIMHD7y8vJKTk1955RXTVYYQ63rXiAwMDJTL5QEBASUlJRMnTkxJSTFRWQiZQq/77u7u7llZWZGRkSqVKjw8fPv27aYoCyFT6MvbTPb29idOnJBKpUajcdWqVcuXL8fFK7IIvTt27+DYsWPvv/++RqOZOnWqTCZzdnZmsTLeqa6G8+ehrAyam8HFBQIC4He/Axsbrsti09mzZz/77DMXF5dFixb5+fn5+PiIRCKui2IV6Z/Lly+7ubkBgJeX161bt/o5Gk9pNCQ2lohEBOCZPyNHkhMnuC6ONVevXrW2tn46G0Kh0NPTMzQ0VCqVymQypVJpMBi4LrNf+ht3Qsi9e/cCAgIAwNnZOT09vf8D8otOR6ZMIQBk+HCydSuRy0lRETl3jixZQqysiEBA9u7lukQWNDc3Ozo6AoC9vf2SJUsiIyO9vLysrDoe6zo6OgYGBi5btiwhISE9Pf3hw4dcF05SGlLmls6V1cl6sjELcSeENDU1RUREMPuD7du3szImX3z+OQEg3t7kwYOOD/3wAxEIiERCSku5qIw1RqMxOjoaACQSSXFxcfvXtVqtUqmUyWRSqTQ0NNTT01MgEHT4BXB2dg4JCYmJiUlISMjOzlapVOyXR4xpjWlxd+PCSsKmFk9dWL5wz6M9Kn3bRNuqt4ECpFXSngzFTtwJIUajUSqVMj+CmJiY1tZWtkbmUksLGTaMAJALFzrfIDqaAJBVq8xaFds2bNgAAE5OTkqlsvsta2trMzIyvv766+XLl4eEhAwaNKhD+gUCwbQPp80qmbW+cv2RuiN5zXmtxn4l4W7r3YmFE0EBzB+BQsD8xSPPI7cpl3AVd8aRI0ckEgkATJs2rb6+nt3BOZCd3XaMbjR2vsG//kUAiJeXectik0wmEwgE1tbWKSkpfXh6ZWXl+fPnExISYmJiQkJC7Ozs3tz1Zns6QQHCa0JPpWdoSai0Siqrkyk1SgPp6QKgQd/gqfQEBfjm+55qOKU2qAkhZdqyNffWWF+znlw02UiMXMadEJKbm+vq6goAo0ePLiwsZH18s9qxgwCQiIguN6irIwBEICBqtRnLYo1cLrezswOAHTt2sDKgTqcrrCuU1ck+qfpkdulsL6WXlcLq6fSDAhx+dggsDFx6Z2lCdUK6Kr1aV93VaKvurgIF+OT71OvrOzyU1pjWZGgivdy7C1lo7jwrKChILpeHh4dfu3YtODj4+PHjU6ZMYX0WM6mpAQDo5uwgZ2ewsYHWVqitBQcHs9XFiqqqqvDw8Obm5g8++CA2NpaVMYVCoY+zjw/4REEU85VW0npbe7tAU5Dfkq9oVhS0FJRry688vnLl8ZX2ZzlbO/tKfP3Efr5i3wC7gHGScY7WjlqiPVB7AAC+cP9isPXgDhPNcJrRl/L69l11z8PDIysra9GiRUlJSTNmzEhISFixYoUpJjI5ZmX2q/VZl1taDo1GEx4eXllZ+eabb+7atct0E9kIbPzEfn5iv/ZfgDp93c2Wm/ma/DxNXn5LvlKjrDfU5zTl5DTlMBu4idzuv3r/evP1RkOjg5XDO07vsFWMSeIOAA4ODidPnty8efPmzZtjY2Pz8vJ27twpFJpqOlNh3jhj9vGdUqmgtfXJlhaCELJ48WK5XO7p6XnixAkb875ZNkQ4ZLLD5MkOk9u/crf1rrJFeVNzU6lRKluUI0QjAKBYWwwAvhJfoYC12JgwfwKBYNOmTT4+PkuWLNmzZ09FRcWxY8cGDx5suhnZcecOHD4MLi7w5z/Dq68CANy40eXGP/8MAPDyy+DoaKby2LBhwwbmXfDU1NShQ4dyXQ6MtBk50mbk205vP/3FRkMjADhbs7kfMfml2QsWLLhw4YKrq+u5c+cmTJhQVFRk6hn7SKOB48chLAxGjYK//Q22bAFCIDAQBg2C0lKQyzt/1tGjAAAz+nIcyRWZTBYfHy8UCmUymbe3N9fldInZqeuJns1B+7wG75W7d+/6+/sDwJAhQy5evGieSXtEryepqWThQmJn13ZqgJ0defddkpbW1nxcvZoAkKAg0tzc8bmXLxORiAiF5Hntav7Izc21tbUFgJ07d3Jdy3Mcrz/OtCC734zjRmRX1Gp1eHg4AAiFQl78rPPziVRKXnyxLeVWViQkhOzeTRobn9msqYmMGUMAyBtvkHPnCPP22cOHJCGBODkRALJ5Myfl90FFRQXTI46NjeW6lucrbilm2vZ1+rpuNuNp3Akher1+7dq1zKsKc82rOWdvU1tLdu8mISFPzvTy8SFSaXcnAlRXt502w7TY7e3b/i6RkPj4Z7Y8eJBoNKb+DvpGrVaPGzcOAKZNm8bNT76XjMQ4WjkaFPBl9ZfdbMbfuDP27dvHtAJmzJjR0NBgplk1GpKcTKKinpzY6OxMYmJIdnaX75h2kJlJPv6YRESQ6dPJwoVk2zZy794zG+zZQwBIYCCpqjLFd9AfBoOBeWn18fGpq+tuZ8krux/tBgU4XXe6+vhqh4daja1ao5bwP+6EkEuXLg0bNgwAxo4dW1ZWZtrJ5HISF0dcXNpSbmNDQkOJTEa0WpYnunmTvPwyASAjRpD//pflwftnzZo1zMLp6TPA+M9IjJGlkaAA22u2K35ZkdyQfPXx1RP1J9ZVrnPLc9tfs59YRNwJIaWlpX5+fgDg4uKSkZHB+vjFxcWGTz4hL7305KBl4kSycyeprWV9ridqasjvf08AiL09f06FT0xMBACRSGSJp2frjLqNVRvtf7bvcCbC4OuD99XsI5YSd0KISqUKCwsDABsbm++++46VMevr6xMTE6dOnSoQCGoCAggA8fAga9eSoiJWxn8+rZa8/37bUb5U2tMjJZPJyclhWjG7du3itpL+UBvUSQ1JCdUJ8Q/idz7cmanOZI5kCCElLSUn60/e0vTo0iIu406eXbzGxcXp9fq+jaPVak+dOjV79mzmvxYAnJycktatI5mZ3AQuIYFYWREAEh3dSQfTXCoqKpiDxlUWfooyWziOO+Pbb79lFq8zZ87s7eJVqVSuXbuW+U8FACsrq6lTpyYmJjY1NZmo2p46e5YMGtR2EHX/vvnnV6vVr732GgBMnz7dIloxZsCLuJPeL17v3buXkJDAdNYYvr6+8fHxVbzqiuTltS0e3N2JXG7OmQ0Gw6xZswBgzJgxA+HCA5bwJe6EkNLSUl9fX2bxmpmZ2ek2zc3NMpksNDS0/SLi4cOHx8XFyc0bpl549IhMnty2eP3pJ7NNu3r1aktsxZgaj+JOCFGpVKGhoQBga2u7f//+9q8bDIbs7OyYmBiH/59TLhaLo6KikpOTLeAqwZYWsnjxk8Wr6R04cIBpxVzo6ppDWvEr7uRXi9ebN29KpdKXXnqp/dA8JCRk9+7djR3e6ue/9sXr/PkmXbxeunSJWa//85//NN0sFop3cWd88803HW7o4+Pj8+mnn1ZUVHBdWj+kpLSdZhMU1Ml9DdhQXl7OLIE+/PBDU4xv6Xgad0LIt99+KxKJHBwcYmJisrOzjVw3sNmRl9d2UpqHB1Eo2B1bpVK9+uqrzNkZ2IrpFH/jfvjwYQCYO3cu14Ww7f59MnEiASCOjnfS0tga1WAwMO/ZYSumG/z95D2lUgkAY8eO5boQtrm5QWYmvPfe+dGjvcLCNm3axMqoH3/88enTp11cXE6fPm0Bl4xxhevfty4xLZoff/yR60JMw2j8Mj6euSnX4sWLW1pa+jPY/v37AUAkEvHr0hn+4W/cX3zxRQAoMtu5Llw4c+aMk5MTAAQHBz/o6+I1OzubacXs3r2b3fIGHp7GXaVSCQQCsVjc57NoLMWNGzeYX2wPD49r16719unl5eXMh2R99NFHpihvgOFp3HNzcwFg/PjxXBdiDlVVVYGBgQDg4OBw6tSpnj9RpVIxa5uZM2cO+P0CK3i6VL158yYAMG21AW/48OFZWVl//OMfm5qaIiMje7h4NRgMCxcuVCqVr7zyytGjRzvcmh11iqdxH7BtmS7Y2tomJibGx8cLBILNmzd/8MEHrczdmrr20UcfnTlzhmnF/PpOvKhzXL+8dO6tt94CgNTUVK4LMbcff/yRuUdpSEhIdXWX9wr97rvvAEAkEpniQrABjKdxZ5Zf9zpc+0yH69evv/DCCwDg6enZ6Q3X//3vfzOXB+zZs8f85Vk0Psb9/v37ADB48GCuC+FMVVXVhAkTAMDBwSE5Ofnph8rKyph9wZo1a7gqz3LxMe7nz58HgEmTJnFdCJc0Gs2iRYsAwNraOv7/d7NpbGxk1jNvv/02tmL6gI9LVaraMl0Ri8UHDx5kgr5u3bqlS5dqNBqmFePr63vkyBFsxfQF179vnViyZAlYwk0MzePYsWPM4tXd3R0Ahg4dWlJSwnVRloqPe3emC0n53r3dvHnzcnJyhgwZUltbKxAIEhISRo0axXVRlop3cTcajQUFBQDA3HQJAUBdXZ1KpWJOI1uxYkVaWhrXFVkq3sW9vLy8qanJ3d19yJAhXNfCC2VlZdHR0Xq9fvXq1e+++25jY2NoaOiWLVu4rssycX001dGpU6cAYObMmVwXwguNjY3Mq9w777yj1+uNRmN8fDzzYdZLly61gMvSeYZ3e3emLUPP6QPdMBgMCxYsyM/P9/PzY1oxAoFg7dq1R48etbOz27t375QpUx49esR1mZaEd3Gn7WyZbqxaters2bOurq5nz55lTotnREVF5eTkjBw58tKlS0FBQbdu3eKwSAvD9ctLR8xrt4Lty5Ytzt69ewFALBbn5uZ2ukFlZeXrr78OAI6OjqdPnzZzeRaKX3HXarU2NjbW1tbN3N1GlA/OnTsnFAoFAsGhQ4e62Yx54wmefecVdYNfcb9x4wYAeHt7c10IlwoLC52dnQFgw4YNz92YWbwy17wuW7YMF6/d41fcv//+ewCYM2cO14Vwpq6ujvnwx8jISIPB0MNnHTt2TCKRAMCkSZMePnxo0gotGr+WqpSvU/V6fVRUVHFx8W9/+9tDhw4xDceemDdvXkZGhpubW3Z2dnBwMC5eu8KvuFPehYyLi7tw4YKbm1tycrK9vX2vnhsYGCiXywMCAkpKSiZOnJiSkmKiIi0b1y8vz2BufVpYWMh1IRzYvn07AIjF4suXL/d5EOZqVwCwtrb+6quvWCxvYOBR3Om52cavtbdiDh8+3M+hDAbD+vXrmcXrmvg1OiPeLPIJHsWdudmGv78/14WYW2FhIXObu40bN7I15tGjR4e+MNRb4T21eGr3nzpNFR4du9N53m9dXV1YWFhDQ8Ps2bPZul8kAERHR59RnGkUNaar04OKgm5rb7M1skXjXdypWqfqdLqoqKjbt2/7+/sfPHiw562YnggcGqgYowiwCyhqKQosDLygvsDi4BaKR3GnsC0TFxd38eJFNze3pKSk3rZiesJd5J7pnRkxOKLeUD+zZOaORztYn8LCcH009QRzgf3du3e5LsRMtm3bBgBisfg///mPSScyEqO0Ssp82HTMnZhWI73vvPIl7g8ePACAQYMGDZBP6XietLQ0phXz/fffm2fGI3VHJD9LQAHTb0+v19ebZ1K+4cvBTPvdB5gO2sBWWFg4f/58vV7/ySefMOd4mcF85/kXRl9wFbmeU52bUDihqKXIPPPyCl/iTk9bpr0VM2fOHKlUas6pg+yD5GPk4+3G39beDi4Ovqi+aM7Z+YBfcR/w61SdTjd37tySkpLx48cnJiaa/6XMQ+SR5Z0VPii8Tl83o2TGzkc7zVwAt/gSd0raMitXrszIyBg+fLiJWjE94WDlcHLUSelwqZ7oY+/GLv9luZ7oOamEA1wvHgghxGg0Ojo6AkBNTQ3XtZjQ1q1bAUAikVy5coXrWggh5Ie6H8Q/i0EBM27PoGTxyou4l5aWAoC7uzvXhZhQWloac231kSNHuK7liZymHNc8V1CAt9K7qGUgfwwWgxcHMwP+SObWrVvR0dEGg2HTpk3z58/nupwngu2D5WPk/nb+xdri4KLgDHVGz58rq5etrlyt1ChNVx7rhFwXADDQ2zK1tbWzZs1qbGycO3fuxo0buS6nIw+RR+bozAUVC842np1VOqt8bPlQ4dD2Ry8/vnxRfbFSV6kjOg+Rx0ynmYH2gcxDqarUA7UHQuxDxkosZj/Fo7gPyL17eysmICCAk1ZMTzhZOyV7Jq+pXDNWMrY962XasvfuvJfTlPP0lpvub/rDoD8ceumQs7UzF5X2F8bdtGJjYzMzM0eMGJGUlMTcyJefrAXWWz22tv+zUlcZUhzyQPfAV+y73m39BPsJEoHkuub6P6r/kdKYsr5y/TcvfMNhtX3H9eKBtLa2MjfbePz4Mde1sOyLL74AAIlEcvXqVa5r6Z2I0ghQQGBhYJOh6emv6436hOqEZkMzIWRxxWJQwE/1P3FUY19wv3cvLCxsbW319vbm886vD1JTU5mrivbv3//GG29wXU4v3Gm9k9yQDAB7Xthjb/XMmwPWAutVw1ZxVBcLuI/7gDySKSgoWLBggcFg+Oyzz6Kjo7kup3cy1ZlGMI6TjHtN8hrXtbCM+0bkwGvLtLdioqKi/vrXv3JdTq8VtBQAwHi78VwXwj7u4z7Amu46nW7OnDmlpaUBAQEHDhzgZyumew2GBgBwEbpwXQj7uI/7ADuY+ctf/pKVlcX/Vkw3BGB5v6I9xHHctVqtXq8Xi8VeXl7cVsKKLVu27N27VyKRJCUlMZ8cZomchc4A8FD3kOtC2MfxUtXW1vaXX35Rq9VCIfeL5n5KTU3dsGGDQCA4cOAAcytqCzVWPBYA5M1yrgthH/cHMwDAnA5p0QoKCubPn28wGP7+97/PmzeP63L65S3Ht4QCYUFLgaJZwXUtLONF3C1dTU1NWFiYSqWaN2/eunXruC6nv0aIRswdPBcAlv+yvNHQ2OFRAoSLotiBcWfBl19+WVZWFhQUxNuzYnrrq5FfeYg8FM2K1wtf31e7r1hbXK2rvvz48ucPPvfK9yrWFnNdYB9Z/BEzH3z66ad2dnbLli0Ti8Vc18KOYcJhuT65f7rzpwx1xtI7S59+yM7KrqilyNvWm6va+kNAiAW/NiFTUzQr0tXpla2VWqJ1FbmOk4yb5jjNydoJANLV6fma/NBBoaNsLeZTvDHuiCJ47I4ognFHFMG4I4pg3BFFMO6IIhh3RBGMO6IIxh1RBOOOKIJxRxTBuCOKYNwRRTDuiCIYd0QRjDuiCMYdUQTjjiiCcUcUwbgjimDcEUUw7ogiGHdEEYw7ogjGHVEE444ognFHFMG4I4pg3BFFMO6IIhh3RBGMO6IIxh1RBOOOKIJxRxTBuCOKYNwRRTDuiCIYd0QRjDuiCMYdUQTjjiiCcUcUwbgjimDcEUUw7ogiGHdEEYw7ogjGHVEE444ognFHFMG4I4pg3BFFMO6IIhh3RBGMO6IIxh1RBOOOKIJxRxTBuCOKYNwRRTDuiCIYd0QRjDuiCMYdUQTjjiiCcUcUwbgjimDcEUUw7ogiGHdEEYw7ogjGHVEE444ognFHFMG4I4pg3BFFMO6IIhh3RJH/Ac/qOOLSUuBLAAAAAElFTkSuQmCC)
Find more compounds similar to Propane, 2,2'-oxybis[1-chloro-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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