- InChI
- InChI=1S/C4H8Cl2O/c5-1-3-7-4-2-6/h1-4H2
- InChI Key
- ZNSMNVMLTJELDZ-UHFFFAOYSA-N
- Formula
- C4H8Cl2O
- SMILES
- ClCCOCCCl
- Molecular Weight1
- 143.01
- CAS
- 111-44-4
- Other Names
-
- 1,1'-Oxybis(2-chloroethane)
- 1,5-Dichloro-3-oxapentane
- 1-Chloro-2-(«beta»-Chloroethoxy)ethane
- 1-Chloro-2-(«beta»-Chloroethoxy)ethane
- 1-chloro-2-(2-chloroethoxy)ethane
- 2,2'-Dichloorethylether
- 2,2'-Dichlor-diaethylaether
- 2,2'-Dichlorethyl ether
- 2,2'-Dichlorodiethyl ether
- 2,2'-Dichlorodiethyl oxide
- 2,2'-Dichloroethyl ether
- 2,2'-Dicloroetiletere
- 2-Chloroethyl ether
- BCEE
- Beta,beta'-dichloroethyl ether
- Bis(chloro-2-ethyl) oxide
- Bis(«beta»-chloroethyl) ether
- Bis(«beta»-chloroethyl) ether
- Chlorex
- Chloroethyl ether
- Clorex
- DCEE
- Di(2-chloroethyl) ether
- Di(«beta»-chloroethyl) ether
- Di(«beta»-chloroethyl) ether
- Dichloroether
- Dichloroethyl ether
- Dichloroethyl oxide
- Diethylene glycol dichloride
- Dwuchlorodwuetylowy eter
- ENT 4,504
- Ethane, 1,1'-oxybis[2-chloro-
- Ether dichlore
- Ether, bis(2-chloroethyl)
- Ether, bis(chloroethyl)
- Khloreks
- NSC 406647
- Oxyde de chlorethyle
- Rcra waste number U025
- UN 1916
- s-Dichloroethyl ether
- sym-Dichloroethyl ether
- «beta»,«beta»'-Dichlorodiethyl ether
- «beta»,«beta»'-Dichloroethyl ether
- «beta»,«beta»'-Dichlorodiethyl ether
- «beta»,«beta»'-Dichloroethyl ether
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔfG° | -146.06 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -289.59 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.68 | kJ/mol | Joback Calculated Property |
| log10WS | -1.12 | Aq. Sol... | |
| logPoct/wat | 1.481 | Crippen Calculated Property | |
| McVol | 97.570 | ml/mol | McGowan Calculated Property |
| Pc | 3488.88 | kPa | Joback Calculated Property |
| Inp | [156.20; 989.00] |
|
|
| Inp | 945.90 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 951.52 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | Outlier 156.20 | NIST | |
| Inp | Outlier 156.20 | NIST | |
| I | [1536.00; 1536.00] |
|
|
| I | 1536.00 | NIST | |
| I | 1536.00 | NIST | |
| I | 1536.00 | NIST | |
| Tboil | [451.00; 452.25] | K |
|
| Tboil | 451.20 | K | NIST |
| Tboil | 451.00 | K | NIST |
| Tboil | 452.25 | K | NIST |
| Tboil | 451.80 ± 0.40 | K | NIST |
| Tboil | 451.00 ± 2.00 | K | NIST |
| Tc | 570.40 | K | Joback Calculated Property |
| Tfus | [223.52; 227.05] | K |
|
| Tfus | 223.52 | K | Aq. Sol... |
| Tfus | 227.05 | K | NIST |
| Tfus | 226.25 ± 0.50 | K | NIST |
| Vc | 0.376 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [161.62; 200.87] | J/mol×K | [388.20; 570.40] |
|
| Cp,gas | 161.62 | J/mol×K | 388.20 | Joback Calculated Property |
| Cp,gas | 168.74 | J/mol×K | 418.57 | Joback Calculated Property |
| Cp,gas | 175.62 | J/mol×K | 448.93 | Joback Calculated Property |
| Cp,gas | 182.28 | J/mol×K | 479.30 | Joback Calculated Property |
| Cp,gas | 188.71 | J/mol×K | 509.67 | Joback Calculated Property |
| Cp,gas | 194.90 | J/mol×K | 540.04 | Joback Calculated Property |
| Cp,gas | 200.87 | J/mol×K | 570.40 | Joback Calculated Property |
| Cp,liquid | [207.81; 253.00] | J/mol×K | [293.15; 295.00] |
|
| Cp,liquid | 207.81 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 253.00 | J/mol×K | 295.00 | NIST |
| η | [0.0003090; 0.0032180] | Pa×s | [216.91; 388.20] |
|
| η | 0.0032180 | Pa×s | 216.91 | Joback Calculated Property |
| η | 0.0017353 | Pa×s | 245.46 | Joback Calculated Property |
| η | 0.0010643 | Pa×s | 274.01 | Joback Calculated Property |
| η | 0.0007158 | Pa×s | 302.56 | Joback Calculated Property |
| η | 0.0005155 | Pa×s | 331.10 | Joback Calculated Property |
| η | 0.0003911 | Pa×s | 359.65 | Joback Calculated Property |
| η | 0.0003090 | Pa×s | 388.20 | Joback Calculated Property |
| ΔfusH | [8.38; 8.39] | kJ/mol | [226.50; 226.50] |
|
| ΔfusH | 8.39 | kJ/mol | 226.50 | NIST |
| ΔfusH | 8.39 | kJ/mol | 226.50 | NIST |
| ΔfusH | 8.38 | kJ/mol | 226.50 | NIST |
| ΔvapH | [45.24; 49.80] | kJ/mol | [273.00; 374.50] |
|
| ΔvapH | 45.24 | kJ/mol | 273.00 | NIST |
| ΔvapH | 49.80 | kJ/mol | 374.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 340.20 | K | 2.00 | NIST |
Similar Compounds
![Ethanol, 2-[2-(2-chloroethoxy)ethoxy]-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAMZklEQVR4nO3cf0zV9R7H8fc5gEzAH91SMpVQiF+FpbZK21oum38oujZZ2jxbbqVbGctqO7Vm6CCjulPWlgxq86JZRlm5yTLiiE3F3Zo/Oio/VCAFAT3Uvan8OnDO6/7xRc5Jk4NwfnB9vx7zn/PlnLM35/v8fD/nwNAEQIh0MId6AKLgYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizJ0UYe6kCHMnRZg7KcLcSRHmToowd1KEuZMizP125HLJmTNy4IC0tYV6lJElPNQDkL/V1UlGhsTGSlycHDggCxbIli1iMoV6rBFhKFd3F1xOOP0+CvnHypVisUhFhRQXi90ulZXyzTehncjlcvX29oZ2BoMJgM879aBn95+7j3ccH2Uatewfy6o6q7b9se2b6SF+EelvXL0q48fLlSsyenTfkYIC2b9fvvwyJOM4nc6CgoKtW7eaTKZHHnkkJydn4sSJIZnE4Pvq3oOeBWcXFDgKEiITosxRC88u7HB3BGGy/zv19fXnzp07dOhQKIdobJQ77/S0LiJxcXL+fEhmKS0tTUtLe/XVV+12u91uLyoqSk5O/uCDD7q6ukIyj4gIfNn5x86kk0k97h7jZo+759v/fPtM3TM+HxgEdXV133333ZYtWxwORwjH6O7uzs/Pj46Ofuihh0Rk/vz5J06cCM0obW2IiIDL5TlSXIwlS4I8RWNjo8ViMQKbMWPGgQMHqqqqMjMzjSNTpkwpLCx0eQ8ZLL5zf/PCm681vuZ9pD93N9yBmsuX/sKioqJEJCYmJjs7u6OjI/iT7NmzJyEhQURMJtPDDz8cExMjIhEREWvWrLl06VLw5qivx9dfA8ADD2D3bs/xxYuxeTPa2vDcc6ipCfQUTqczPz/feBGio6Ozs7O7u7v7v1peXm5cEURk9uzZFRUVgZ7nOr5zX3Vu1frm9d5HjNz3X9k/u3r2vsv7AjbbTXkXtmTJkqeeesp4BePi4rZv3x60y4b3NSwlJeXHH38E4HA4srKywsPDg7cInU7k5yMmBqNHo6EBNhsmTMC77+Kzz7BsGWbORGcnXn8dIoiIwMsvI2CLsLy8PCUlxXhBFi1a1NjYeON9XC5XSUnJvffea9wtyDuh79xzW3Kf/+157yNG7hlnM+SIyBFZfHZxdWd1wCb8ixt3SeN4eXn5zJkz+y8b+/YFdhEOfA0DUF1dfd3e3dvbG5BRSkuRmAgRmEywWHDxIgCcOYOPP8a6ddi5E52dAOBwICsL4eEQQUwMsrPh10XofV6Sk5ONlT+A9vb2nJycMWPGiEj81Km9a9b0TR5gvnOv6qwad3xcbVetcbPb3W3k3u5qz2vNG3d8nByR8KPhq86tanG2BG7Q6wrLy8vr6enxvoPb7S4pKYmPj++/bNjt9kBMMphrmMFms/UvwlmzZvl5ETY2wmKBCESQnAxfhQFAdTUyM/seMmUKCgsx7EXoc+UPoLW1dfXq1cVPPAERjB2LjRv9uwhv5Dt3AB9d+mjCrxMyzmYsOrtoRtWMXX/s6v+o2tbTltWYFX40XI5I9LFoa5P1iuuK36ccfGHt7e25ubnGZSM8PPy1rCx/XjYaGjpWrLgrKkpE0tPTf/rpJ5+PCMgi7H/3IoLoaGRnY9CFAYDNhlmz+qK//36Ulg55EJvNlpqa2n9ezp8/P5RnqanxLMLJk/2yCG9mULkD6HR1Hus4dqrzlNPtvOq62uxs9v5qTWdNZn2m8d5msn1yoaOw1+2fiW91lzS0tbVZrdZRo0ate/JJREfDasWV4S3Cri7k5CAqCiL/XrBg8+bN1+0tA+vo6MjLyxs3bpyImM1mi8XS0jLUndBmQ2pqXxyLFmFohblcKC7G1KnG87S+8MKpU6du6Qmampq8z0tZWdlQxvDmv0U4gMHmPhiVVyvn1Mwxok87lVb632FNPJxd0lBVVXXZe+/+178wtE+xfinMaxEa35HVar18+fLgH24UtnPu3L53L8MvrLsb+fkYP351evrgF+Hwz8tNud0oKcG0aX0v9fz5+PVX/zzzNf7MHYALru2/b487ESdH5O5jdy/JXHLy5MkhPI9/dklDZSWMRESQloY9e27hsU1Nf3l/PPzCgJqamv5PsZMnTx7Mp9iurq7c3FzjR64piYmuTZtwK3vLwDouXnzppZeMHyWNGTMmJyenvb39Zne22WxpaWn+OS83HagDGzdi7FiIIDwcW7YAQEEBUlORkIDERKxdi+5u7NqFZ5/1PGrrVrz4os/n9nPufQO7Ot5reW/+P+eLSFhY2KpVqwa/d/t/l8SQLhvDfH/sS2Vl5dy5c41vMy0tbc/NF2EwCgNqa2sHXoTe5yUpKemHH34IxBgebW2wWhEVhRMnUFaG6dNRVwcAf/6Jp5/G+vXYuRMZGZ77FxZixQqfzxqQ3A3G3h0ZGTnIvTuAu6Th2t4NEZjNsFjQ3AwALS0oKsLbb+OTT/p+Jn3wIJKS+tbG8uW4cMGfY1xjfIqdPn16/6fY48ePe98h2IUBhw8fvnERGufF+PQfkPMyAON0ZGSgqMhz0G7HXXeNuNwNxmXDZDKJyD333HOzvduf714G9vvvsFoRGQkRlJaithaxsbBasWMH1q7FpEmor8fPP8NsRlISAl+Y8evh8ePH93+KbW5uDmFhbrd7x44d/b8GmjNnjvEbPRFZtmzZhcCsfB9SUnDwoOdmTw/CwvDpp4iNxcKFff/S00dE7obDhw8//vjjxquWmppaUlLS/6XgX8MAoLYW2dkAsHQp3n/fc/ydd2CxAMD338PpDMYkAACHw/HKK69EREQYfU+aNCm0hfUvwrFjx4aFhSUlJe3duzf4Y/SZORM2m+dmezvMZmzbhnnzUFXV92/DhhGUO/5u7/7ll18C++5lMGJjUVvruXn0KOLjgz3DNadPn87MzDSbzenp6SEuDADgcDgqKirKysqcQVz5f2PlSmzY4Lm5dy/S0kbom5nrdHV1ffjhh3fccYfxayAj/eXLl4dml3S7ERGB1lbPkd9+Q0xMCCbxcvr06aamphAXNqLU1mLiRGzbhqYmlJcjMRFffTW03IP9x3uRkZFvvPHGypUrc3Jyent77Xb7hg0b5s2bF+Qx+phMEhcn585JbGzfkYYGmTYtNMNcc99994V2gBEnKUn27pWCAikqkqlTZdMmyciQQ4fkscc894mPlw7ff4YxqL9mup2tWydnzsjnn4vZLL29snSpPPqovPVWqMeigFCf+9WrsnSptLbKgw/K0aOSkCBffPGXvwai24j63A0XLkhDgyQkyLUfidBtibmTIvxvlUgR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynC3EkR5k6KMHdShLmTIsydFGHupAhzJ0WYOynyPyArinCPSlWsAAAAAElFTkSuQmCC)
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